WO2024077901A1 - 一种工业固废碳化固化免烧砌块及制备方法 - Google Patents

一种工业固废碳化固化免烧砌块及制备方法 Download PDF

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WO2024077901A1
WO2024077901A1 PCT/CN2023/087438 CN2023087438W WO2024077901A1 WO 2024077901 A1 WO2024077901 A1 WO 2024077901A1 CN 2023087438 W CN2023087438 W CN 2023087438W WO 2024077901 A1 WO2024077901 A1 WO 2024077901A1
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building block
solid waste
industrial solid
blast furnace
water
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PCT/CN2023/087438
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English (en)
French (fr)
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李勖晟
刘松玉
童立元
袁校柠
钱淼
李迪
王正成
林江源
郑芝芸
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东南大学
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Publication of WO2024077901A1 publication Critical patent/WO2024077901A1/zh

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Classifications

    • 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
    • C04B30/00—Compositions for artificial stone, not containing binders
    • 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
    • C04B18/00—Use of agglomerated or waste materials or refuse as fillers for mortars, concrete or artificial stone; Treatment of agglomerated or waste materials or refuse, specially adapted to enhance their filling properties in mortars, concrete or artificial stone
    • C04B18/04—Waste materials; Refuse
    • C04B18/0481—Other specific industrial waste materials not provided for elsewhere in C04B18/00
    • 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
    • C04B18/00—Use of agglomerated or waste materials or refuse as fillers for mortars, concrete or artificial stone; Treatment of agglomerated or waste materials or refuse, specially adapted to enhance their filling properties in mortars, concrete or artificial stone
    • C04B18/04—Waste materials; Refuse
    • C04B18/14—Waste materials; Refuse from metallurgical processes
    • C04B18/141—Slags
    • C04B18/142—Steelmaking slags, converter slags
    • 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
    • C04B40/00—Processes, in general, for influencing or modifying the properties of mortars, concrete or artificial stone compositions, e.g. their setting or hardening ability
    • C04B40/02—Selection of the hardening environment
    • C04B40/0231—Carbon dioxide hardening
    • C04B40/0236—Carbon dioxide post-treatment of already hardened material
    • 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
    • C04B2201/00—Mortars, concrete or artificial stone characterised by specific physical values
    • C04B2201/20—Mortars, concrete or artificial stone characterised by specific physical values for the density
    • 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
    • C04B2201/00—Mortars, concrete or artificial stone characterised by specific physical values
    • C04B2201/50—Mortars, concrete or artificial stone characterised by specific physical values for the mechanical strength
    • Y—GENERAL 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
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W30/00—Technologies for solid waste management
    • Y02W30/50—Reuse, recycling or recovery technologies
    • Y02W30/91—Use of waste materials as fillers for mortars or concrete

Definitions

  • the invention relates to an industrial solid waste carbonization solidification non-fired building block and a preparation method thereof, belonging to the technical field of civil engineering materials.
  • Patent CN 112279671 A uses polystyrene foam particles, solid wastes such as steel slag and desulfurized gypsum, as well as cement and other materials to prepare concrete blocks, effectively utilizing a variety of industrial solid wastes.
  • solid wastes such as steel slag and desulfurized gypsum
  • cement and other materials to prepare concrete blocks, effectively utilizing a variety of industrial solid wastes.
  • a certain amount of cement is still used in the production process, indirectly causing a large amount of carbon emissions.
  • Patent CN 112479667 A uses a variety of industrial solid wastes and phosphogypsum-based cement, which are pressed and cured for 28 days to prepare blocks. The curing age is relatively long, which limits the improvement of production efficiency.
  • Patent CN 102786320 A uses autoclaving and aeration technology to prepare concrete blocks made mainly of industrial waste, rare earths, industrial hydrogen peroxide and other materials. Although autoclaving can effectively improve the strength of blocks, it still consumes fossil energy and does not meet the requirements of green environmental protection.
  • the present invention provides an industrial solid waste carbonization solidification unfired building block and a preparation method thereof.
  • the present invention adopts the following technical scheme
  • the industrial solid waste carbonized solidified unfired building block of the present invention has the following mass proportion of raw materials:
  • the industrial solid waste carbonization solidification unfired building blocks of the present invention have carbide slag as main mineral components of calcium oxide and silicon dioxide, and contain a small amount of oxides of potassium, sodium and iron metal elements; the carbide slag needs to be pre-treated by ball milling to make its specific surface area not less than 250m2 /kg.
  • the industrial solid waste carbonization solidification unfired building blocks of the present invention mainly contain calcium oxide, silicon dioxide, aluminum oxide and magnesium oxide as the main mineral components of blast furnace slag; and contain a small amount of oxides of iron and titanium metal elements; the blast furnace slag needs to be pre-treated by ball milling to make its surface area not less than 250m2 /kg.
  • the industrial solid waste carbonized solidified unfired building blocks of the present invention is tap water, purified water or distilled water.
  • the industrial solid waste carbonization solidification unfired building block of the present invention is filled with CO2 in a high-pressure steel cylinder container.
  • a method for preparing industrial solid waste carbonization solidification unfired building blocks the preparation steps are as follows:
  • Raw material preparation weigh carbide slag, blast furnace slag, water and CO 2 according to the mix ratio;
  • slurry preparation carbide slag and blast furnace slag are put into a stirring device according to a proportion and stirred, and water is added in portions during the stirring process until the water is added to form a slurry;
  • the method for preparing the industrial solid waste carbonized solidified unfired building blocks of the present invention comprises the following steps: after the carbide slag and blast furnace slag are added to the stirring device in S2, the stirring device stirs for 1-2 minutes at a speed greater than 100 r/min to fully mix them; water is added to the mixture of the carbide slag and blast furnace slag in batches, and the mixture is stirred for 1-2 minutes after each addition of water until the water addition is completed.
  • the stirring process it is noted that the solid waste cannot sink to the bottom or agglomerate, and the slurry is ensured to be uniform and free of sediment.
  • the CO2 equipment in S5 is a curing room or a curing box; the curing conditions are: CO2 concentration (volume fraction) is not less than 20%, temperature is 20-25°C, relative humidity is 50-75%, and curing time is 24-96h.
  • the industrial solid waste carbonization solidification unfired building blocks are based on the idea of treating waste with waste, and all raw materials except water are bulk waste generated by industrial production: the pH value of carbide slag is about 13, and it can absorb a large amount of CO2 during the carbonization process, and provide an alkaline environment for the active components in blast furnace slag; the main components of blast furnace slag can undergo hydration, volcanic ash and gelation reactions, which can better enhance the strength of the building blocks; the addition of CO2 transforms the alkaline substances in the building blocks into carbonates with greater strength and volume, fills the pores in the building blocks, and further improves the strength of the building blocks.
  • the preparation method of industrial solid waste carbonization solidification unburned blocks adopted by the present invention utilizes the characteristics of carbide slag and blast furnace slag that can efficiently absorb CO2 and the high strength of their products to replace the original calcination link, which not only avoids the use of cement and fossil fuels and reduces CO2 emissions, but also can consume a large amount of this greenhouse gas, providing a new method for energy conservation and emission reduction, and effectively helping to achieve the goal of "carbon neutrality" as soon as possible.
  • the industrial solid waste carbonization solidification unburned blocks prepared by this method have a short production cycle.
  • the compressive strength of the blocks can be effectively and quickly improved, so that the entire curing cycle is controlled within 2 to 5 days, compared with the traditional block preparation which only requires 7 to 28 days in the curing link, which greatly improves the production efficiency.
  • the present invention is easy to operate and requires less mechanical equipment.
  • FIG1 is a flow chart of the method for preparing industrial solid waste carbonization solidification unfired building blocks of the present invention.
  • FIG2 is a stress-strain curve diagram of the block of Example 1-2 of the present invention in the unconfined compressive strength test
  • FIG3 is a stress-strain curve diagram of the block of Example 3-4 of the present invention in the unconfined compressive strength test
  • FIG. 4 is a stress-strain curve diagram of the block of Example 5-6 of the present invention in the unconfined compressive strength test.
  • Example 1 An industrial solid waste carbonization solidification unburned building block, the materials are selected according to the following mass fractions:
  • Raw material preparation weigh corresponding proportions of carbide slag, blast furnace slag, water and CO 2 and set aside.
  • Slurry preparation put carbide slag and blast furnace slag into a stirring device and stir at a speed of 100r/min for 2 minutes to mix them evenly. After fully mixing, divide the water into 3 parts and add them to the mixture in batches. Stir for 2 minutes after each addition of water until the addition is complete to ensure that the slurry is uniform and has no sediment.
  • Curing and demoulding Place the mold after pouring the slurry in a standard curing environment for 24 hours, and then demould it.
  • Carbonization curing the demoulding body is immediately placed in a carbonization box for curing.
  • the curing conditions are CO2 concentration (volume fraction) 20%, temperature 20°C, relative humidity 50%, and carbonization time is 24h.
  • the finished blocks were tested and found to have a dry density of 1167 kg/m 3 , an unconfined compressive strength of 4.83 MPa, a carbonization coefficient of 0.91, and a drying shrinkage of 0.060%.
  • Example 2 The only difference between this example and Example 1 is that the carbonization time is 48 hours.
  • the finished blocks were tested and found to have a dry density of 1208 kg/m 3 , an unconfined compressive strength of 5.50 MPa, a carbonization coefficient of 0.95, and a drying shrinkage of 0.057%.
  • Embodiment 3 This embodiment is different from the embodiment except that the content of calcium carbide slag is 200 parts and the content of blast furnace slag is 400 parts.
  • the finished blocks were tested and found to have a dry density of 1247 kg/m 3 , an unconfined compressive strength of 6.03 MPa, a carbonization coefficient of 0.92, and a drying shrinkage of 0.032%.
  • Example 4 The only difference between this example and Example 3 is that the carbonization time is 96 hours.
  • the finished blocks were tested and found to have a dry density of 1285 kg/m 3 , an unconfined compressive strength of 6.66 MPa, a carbonization coefficient of 0.95, and a drying shrinkage of 0.028%.
  • Embodiment 5 the difference between this embodiment and embodiment 1 is only that the content of calcium carbide slag is 200 parts, and the content of blast furnace slag is 400 parts.
  • the finished blocks were tested and found to have a dry density of 1242 kg/m 3 , an unconfined compressive strength of 5.80 MPa, a carbonization coefficient of 0.89, and a drying shrinkage of 0.011%.
  • Example 6 The only difference between this example and Example 5 is that the carbonization time is 96 hours.
  • the finished blocks were tested and found to have a dry density of 1228 kg/m 3 , an unconfined compressive strength of 7.84 MPa, a carbonization coefficient of 0.90, and a drying shrinkage of 0.009%.
  • Example 1 of the present invention can reach MU3.5 grade
  • Examples 2, 3, 4, and 5 can reach MU5 grade
  • Example 6 can reach MU7.5 grade.

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  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Ceramic Engineering (AREA)
  • Materials Engineering (AREA)
  • Structural Engineering (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Environmental & Geological Engineering (AREA)
  • Civil Engineering (AREA)
  • Health & Medical Sciences (AREA)
  • Toxicology (AREA)
  • Processing Of Solid Wastes (AREA)

Abstract

本发明涉及一种工业固废碳化固化免烧砌块及制备方法，属于土木建筑工程材料技术领域。该工业固废碳化固化免烧砌块的原料的质量份数配合比为：电石渣：250份-400份；高炉矿渣：250份-400份；水：250份-350份；CO2：50份-100份。本发明基于以废治废的思路，原料除水外全部为工业生产所产生的大宗废物：电石渣的pH值在13左右，在碳化过程中能吸收大量CO2，并为高炉矿渣中的活性成分提供了碱性环境；高炉矿渣的主要成分能够发生水化、火山灰和胶凝反应，较好地增强砌块的强度；CO2的加入使得砌块中的碱性物质转变为强度和体积均较大的碳酸盐，填补了砌块孔隙，使得砌块强度进一步提高。

Description

一种工业固废碳化固化免烧砌块及制备方法 技术领域
本发明涉及一种工业固废碳化固化免烧砌块及制备方法，属于土木建筑工程材料技术领域。
背景技术
据不完全统计，目前全国累计堆存的工业固体废物超过300亿吨，年增量约41.4亿吨，且缺乏有效的资源化利用手段。这些工业固废的堆存侵占土地，污染毒化土壤、水体和大气，严重影响生态环境，造成明显或潜在的经济损失和资源浪费。其实，许多工业固废具有良好的工程性质，加以处理后能够制备高质量的建筑材料，如乙烯工业产生的电石渣能够提供大量的钙和碱性环境、炼铁产生的高炉矿渣能够对水泥起到一定的替代作用，具备很好的应用潜力。
当下，制备建筑砌块已成为消纳工业固废的重要手段之一，已有部分科研工作者开展了相关的研究。
专利CN 112279671 A采用了聚苯乙烯泡沫粒和钢渣、脱硫石膏等固废以及水泥等材料制备混凝土砌块，有效利用了多种工业固废，但生产过程中仍会使用一定量的水泥，间接造成大量的碳排放。
专利CN 112479667 A采用多种工业固废和磷石膏基水泥，经过压制后养护28天制备砌块，其养护龄期较长，限制了生产效率的提高。
专利CN 102786320 A则通过蒸压加气技术，制备了以工业废弃物、稀土、工业双氧水等材料为主的混凝土砌块。虽然蒸压可以有效提升砌块强度，仍然需要消耗化石能源，不符合绿色环保的要求。
但是，砌块的生产仍然存在着几个典型的问题。首先，现有的生产技术都几乎需要加入水泥，而水泥的生产是CO2的重要来源之一。2020年，我国水泥工业产生的CO2排放量约13亿吨，约占建材行业总碳排放的80％，全国总碳排放的12％，大量利用水泥同“碳中和”、“碳达峰”理念相悖。其次，部分砌块制备仍采用煅烧的方法，工艺复杂且设备众多的同时，还会造成能源的消耗和CO2的排放。此外，砌块多需要进行长时间的养护，一般为28天，少数为7天，整体的生产效率受到了限制。
发明内容
本发明针对上述问题提供了一种工业固废碳化固化免烧砌块及制备方法。
本发明采用如下技术方案
本发明所述的工业固废碳化固化免烧砌块，该工业固废碳化固化免烧砌块的原料的质量份数配合比如下：
电石渣：250份-400份；
高炉矿渣：250份-400份；
水：250份-350份；
CO2：50份-100份。
本发明所述的工业固废碳化固化免烧砌块，所述的电石渣主要矿物成分为氧化钙、二氧化硅，含有少量钾、钠、铁金属元素的氧化物；电石渣需经过球磨等预处理，使其比表面积不低于250m2/kg。
本发明所述的工业固废碳化固化免烧砌块，所述的高炉矿渣主要矿物成分为氧化钙、二氧化硅、三氧化二铝、氧化镁；含有少量铁、钛金属元素的氧化物；高炉矿渣需经过球磨等预处理，使其表面积不低于250m2/kg。
本发明所述的工业固废碳化固化免烧砌块，所述的水为自来水或净水或蒸馏水。
本发明所述的工业固废碳化固化免烧砌块，所述的CO2采用高压钢瓶制式容器灌装。
一种工业固废碳化固化免烧砌块的制备方法，制备步骤如下：
S1、原料准备：按照配合比称取电石渣、高炉矿渣、水、CO2；
S2、浆体制备：将电石渣和高炉矿渣按照比例投入搅拌装置进行搅拌，在搅拌过程中分次加入水，直至水添加完形成浆体；
S3、浇筑成型：将S2中形成的浆体立即倒入模具中浇筑成型；
S4、养护脱模：将浇筑浆料后的模具放在标准养护环境中养护12～24h，之后进行脱模；
S5、碳化固化：将S4中脱模后的坯体立即放入CO2设备中养护、固化；形成砌块。
本发明所述的工业固废碳化固化免烧砌块的制备方法，所述S2中的当电石渣和高炉矿渣添加搅拌装置后，搅拌装置以大于100r/min的转速搅拌1-2mins，使其充分混合后；向电石渣和高炉矿渣的混合料中分次加入水，每次加入水后再搅拌1-2mins，直至完成水添加。搅拌过程中注意固废不能沉底、结团，确保浆体均匀、无沉积。
本发明所述的工业固废碳化固化免烧砌块的制备方法，所述的S5中CO2设备为养护室或养护箱；养护条件为：CO2浓度(体积分数)不低于20％，温度20～25℃，相对湿度50～75％，养护时间为24～96h。
有益效果
本发明提供的工业固废碳化固化免烧砌块，基于以废治废的思路，原料除水外全部为工业生产所产生的大宗废物：电石渣的pH值在13左右，在碳化过程中能吸收大量CO2，并为高炉矿渣中的活性成分提供了碱性环境；高炉矿渣的主要成分能够发生水化、火山灰和胶凝反应，较好地增强砌块的强度；CO2的加入使得砌块中的碱性物质转变为强度和体积均较大的碳酸盐，填补了砌块孔隙，使得砌块强度进一步提高。
传统的砌块制备一般要运用到大量水泥并进行煅烧或高温加热，而水泥生产过程也会产生的巨大能耗以及大量CO2、SO2和粉尘等有毒物质的排放；煅烧和高温加热同时会消耗大量资源并产生CO2。本发明采用的工业固废碳化固化免烧砌块的制备方法，利用了电石渣和高炉矿渣能够高效吸收CO2、其产物强度高的特点代替原有的煅烧环节，不仅避免了使用水泥、化石燃料，减少CO2排放，而且还能够大量消耗这一温室气体，为节能减排提供了新方法，有效助力“碳中和”目标的早日达成。
通过该方法所制备的工业固废碳化固化免烧砌块，生产周期短，通过在高浓度CO2环境中进行养护，能够有效、迅速地提高砌块的抗压强度，使得整个养护周期控制在为2～5天内，相较于传统的砌块制备仅在养护环节就需要7～28天，大大提高了生产效率。且本发明操作简便，所需机械器材较少。
附图说明
图1为本发明的工业固废碳化固化免烧砌块制备方法的流程图。
图2为本发明按实施例1-2的砌块在无侧限抗压强度测试中的应力-应变曲线图；
图3为本发明按实施例3-4的砌块在无侧限抗压强度测试中的应力-应变曲线图；
图4为本发明按实施例5-6的砌块在无侧限抗压强度测试中的应力-应变曲线图。
具体实施方式
为使本发明实施例的目的和技术方案更加清楚，下面将结合本发明实施例的附图，对本发明实施例的技术方案进行清楚、完整地描述。显然，所描述的实施例是本发明的一部 分实施例，而不是全部的实施例。基于所描述的本发明的实施例，本领域普通技术人员在无需创造性劳动的前提下所获得的所有其他实施例，都属于本发明保护的范围。
实施例1：一种工业固废碳化固化免烧砌块，按照以下质量份数选取材料：
电石渣400份，高炉矿渣200份，水300份，CO2100份。电石渣和高炉矿渣的组成成分如表1所示。
表1电石渣和高炉矿渣的主要组成成分(质量分数％)
采用如下步骤制备工业固废碳化固化免烧砌块：
S1、原料准备：称取对应比例的电石渣、高炉矿渣、水和CO2，备用。
S2、浆体制备：将电石渣和高炉矿渣投入搅拌装置，以100r/min的转速搅拌2mins，使其混合均匀。使其充分混合后，将水分成3份，向混合料中分次加入，每次加水后需搅拌2mins，直至添加完毕，保证浆体均匀、无沉积。
S3、浇注成型：立即将制备的浆体倒入模具中浇筑成型。
S4、养护脱模：将浇筑浆料后的模具放在标准养护环境中养护24h，之后进行脱模。
S5、碳化固化：将脱模后的坯体立即放入碳化箱中养护，养护条件为CO2浓度(体积分数)20％，温度20℃，相对湿度50％，碳化时间为24h。
制成的成品砌块经检测，干密度为1167kg/m3，无侧限抗压强度为4.83MPa，碳化系数为0.91，干燥收缩率为0.060％。
实施例2：本实施例与实施例1的区别仅在于碳化时间为48h。
制成的成品砌块经检测，干密度为1208kg/m3，无侧限抗压强度为5.50MPa，碳化系数为0.95，干燥收缩率为0.057％。
实施例3：本实施例与实施例仅在于电石渣含量为200份，高炉矿渣含量为400份。
制成的成品砌块经检测，干密度为1247kg/m3，无侧限抗压强度为6.03MPa，碳化系数为0.92，干燥收缩率为0.032％。
实施例4：本实施例与实施例3的区别仅在于碳化时间为96h。
制成的成品砌块经检测，干密度为1285kg/m3，无侧限抗压强度为6.66MPa，碳化系数为0.95，干燥收缩率为0.028％。
实施例5：本实施例与实施例1的区别仅在于电石渣含量为200份，高炉矿渣含量为400份。
制成的成品砌块经检测，干密度为1242kg/m3，无侧限抗压强度为5.80MPa，碳化系数为0.89，干燥收缩率为0.011％。
实施例6：本实施例与实施例5的区别仅在于碳化时间为96h。
制成的成品砌块经检测，干密度为1228kg/m3，无侧限抗压强度为7.84MPa，碳化系数为0.90，干燥收缩率为0.009％。
以GB/T8239-2014、JC/T 862-2008等近似产品的国家、行业标准作为参考，本发明的实施例1可达到MU3.5等级，实施例2、3、4、5可达到MU5等级，实施例6可达到MU7.5等级。
以上所述，仅为本发明较佳的具体实施方式，但本发明的保护范围并不局限于此，任何熟悉本技术领域的技术人员在本发明揭露的技术范围内，可轻易想到的变化或替换，都应涵盖在本发明的保护范围之内。因此，本发明的保护范围应该以权利要求的保护范围为准。

Claims (8)

  1. 一种工业固废碳化固化免烧砌块，其特征在于：该工业固废碳化固化免烧砌块的原料的质量份数配合比如下：
    电石渣：250份-400份；
    高炉矿渣：250份-400份；
    水：250份-350份；
    CO2：50份-100份。
  2. 根据权利要求1所述的工业固废碳化固化免烧砌块，其特征在于：所述的电石渣主要矿物成分为氧化钙、二氧化硅、钾、钠、铁的氧化物；电石渣需经过球磨等预处理，使其比表面积不低于250m2/kg。
  3. 根据权利要求1所述的工业固废碳化固化免烧砌块，其特征在于：所述的高炉矿渣主要矿物成分为氧化钙、二氧化硅、三氧化二铝、氧化镁、铁、钛的氧化物；高炉矿渣需经过球磨等预处理，使其表面积不低于250m2/kg。
  4. 根据权利要求1所述的工业固废碳化固化免烧砌块，其特征在于：所述的水为自来水或净水或蒸馏水。
  5. 根据权利要求1所述的工业固废碳化固化免烧砌块，其特征在于：所述的CO2采用高压钢瓶制式容器灌装。
  6. 一种工业固废碳化固化免烧砌块的制备方法，其特征在于：制备步骤如下：
    S1、原料准备：按照配合比称取电石渣、高炉矿渣、水、CO2；
    S2、浆体制备：将电石渣和高炉矿渣按照比例投入搅拌装置进行搅拌，在搅拌过程中分次加入水，直至水添加完形成浆体；
    S3、浇筑成型：将S2中形成的浆体立即倒入模具中浇筑成型；
    S4、养护脱模：将浇筑浆料后的模具放在标准养护环境中养护12～24h，之后进行脱模；
    S5、碳化固化：将S4中脱模后的坯体立即放入CO2设备中养护、固化；形成砌块。
  7. 根据权利要求5所述的工业固废碳化固化免烧砌块的制备方法，其特征在于：所述S2中的当电石渣和高炉矿渣添加搅拌装置后，搅拌装置以大于100r/min的转速搅拌1-2mins，使其充分混合后；向电石渣和高炉矿渣的混合料中分次加 入水，每次加入水后再搅拌1-2mins，直至完成水添加。
  8. 根据权利要求5所述的工业固废碳化固化免烧砌块的制备方法，其特征在于：所述的S5中CO2设备为养护室或养护箱；养护条件为：CO2浓度不低于20％，温度20～25℃，相对湿度50～75％，养护时间为24～96h。
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