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CN114409425B - A kind of preparation method of rich porous high water absorption ceramsite based on sludge - Google Patents

A kind of preparation method of rich porous high water absorption ceramsite based on sludge Download PDF

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CN114409425B
CN114409425B CN202210091176.7A CN202210091176A CN114409425B CN 114409425 B CN114409425 B CN 114409425B CN 202210091176 A CN202210091176 A CN 202210091176A CN 114409425 B CN114409425 B CN 114409425B
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ceramsite
sludge
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glass powder
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CN114409425A (en
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孟军平
崔振霄
梁金生
王亚平
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Hebei University of Technology
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    • CCHEMISTRY; METALLURGY
    • C04CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
    • C04BLIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
    • C04B38/00Porous mortars, concrete, artificial stone or ceramic ware; Preparation thereof
    • C04B38/009Porous or hollow ceramic granular materials, e.g. microballoons
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    • C04CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
    • C04BLIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
    • C04B33/00Clay-wares
    • C04B33/02Preparing or treating the raw materials individually or as batches
    • C04B33/13Compounding ingredients
    • C04B33/131Inorganic additives
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    • C04CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
    • C04BLIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
    • C04B33/00Clay-wares
    • C04B33/02Preparing or treating the raw materials individually or as batches
    • C04B33/13Compounding ingredients
    • C04B33/132Waste materials; Refuse; Residues
    • C04B33/1321Waste slurries, e.g. harbour sludge, industrial muds
    • CCHEMISTRY; METALLURGY
    • C04CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
    • C04BLIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
    • C04B33/00Clay-wares
    • C04B33/02Preparing or treating the raw materials individually or as batches
    • C04B33/13Compounding ingredients
    • C04B33/132Waste materials; Refuse; Residues
    • C04B33/1328Waste materials; Refuse; Residues without additional clay
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    • C04CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
    • C04BLIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
    • C04B33/00Clay-wares
    • C04B33/02Preparing or treating the raw materials individually or as batches
    • C04B33/13Compounding ingredients
    • C04B33/132Waste materials; Refuse; Residues
    • C04B33/135Combustion residues, e.g. fly ash, incineration waste
    • C04B33/1355Incineration residues
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    • C04B33/00Clay-wares
    • C04B33/02Preparing or treating the raw materials individually or as batches
    • C04B33/13Compounding ingredients
    • C04B33/132Waste materials; Refuse; Residues
    • C04B33/138Waste materials; Refuse; Residues from metallurgical processes, e.g. slag, furnace dust, galvanic waste
    • CCHEMISTRY; METALLURGY
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    • C04BLIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
    • C04B2235/00Aspects relating to ceramic starting mixtures or sintered ceramic products
    • C04B2235/02Composition of constituents of the starting material or of secondary phases of the final product
    • C04B2235/30Constituents and secondary phases not being of a fibrous nature
    • C04B2235/36Glass starting materials for making ceramics, e.g. silica glass
    • 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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  • Ceramic Engineering (AREA)
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  • Treatment Of Sludge (AREA)

Abstract

本发明公开了一种基于污泥的富孔高吸水率陶粒的制备方法,以污泥与生活垃圾焚烧炉渣为主要原料,添加适量玻璃粉,通过调控主要组分质量比为:SiO2/Al2O3=2.3~3.4,(SiO2+Al2O3)/(CaO+K2O+MgO)=1.7~3.8,来控制焙烧过程液相的生成量,从而提高陶粒的筒压强度,降低焙烧温度。将满足上述组分质量比的生活垃圾焚烧炉渣、污泥、玻璃粉和水混合均匀,经造粒、干燥后,在1000~1080℃温度下焙烧20~50min,即可得到性能优异的陶粒。本发明具有工艺简单、生产成本低、资源利用率高、环境友好等诸多优点,不仅可同步实现污泥的彻底解毒和资源化高效利用,而且可为陶粒工业提供原料,减少对天然原料的依赖。The invention discloses a method for preparing ceramsite with rich pores and high water absorption rate based on sludge. The main raw materials are sludge and domestic waste incineration slag, and an appropriate amount of glass powder is added. The mass ratio of the main components is adjusted to be: SiO 2 / Al 2 O 3 =2.3~3.4, (SiO 2 +Al 2 O 3 )/(CaO+K 2 O+MgO)=1.7~3.8, to control the amount of liquid phase generated during the roasting process, thereby increasing the cylinder pressure of ceramsite strength, reduce the firing temperature. Mix the domestic waste incineration slag, sludge, glass powder and water that satisfy the mass ratio of the above components evenly, granulate and dry, and then roast at 1000-1080°C for 20-50 minutes to obtain ceramsite with excellent properties . The present invention has many advantages such as simple process, low production cost, high utilization rate of resources, and environmental friendliness. rely.

Description

一种基于污泥的富孔高吸水率陶粒的制备方法A kind of preparation method of rich porous high water absorption ceramsite based on sludge

技术领域technical field

本发明属于水污染净化材料领域,涉及污泥资源化利用,具体涉及一种基于污泥的富孔高吸水率陶粒的制备方法,实现污泥的重金属固化与资源化利用。The invention belongs to the field of water pollution purification materials, and relates to sludge resource utilization, in particular to a method for preparing sludge-based ceramsite with rich pores and high water absorption rate, so as to realize heavy metal solidification and resource utilization of sludge.

背景技术Background technique

市政污泥是污水厂在处理城市生活污水和工业废水过程中产生的带有大量污染物的副产物。从外观上看,城市污泥是呈黑色或黑褐色的半流体状或泥饼状的絮凝体,是由泥砂、纤维、动植物残体以及多种微生物形成的菌胶团,同时含有铜、砷、铅、锌、铬、镉等重金属和难降解的有机、无机污染成分。其特点为:①含水率很高,持水力强,难以压缩脱水;②稳定性极差,易变质,产生恶臭;③呈现介于流体和胶体之间的絮凝体状态,流动性差;④含有多种重金属成分,简单处理会造成重金属污染;⑤产量大,处理成本高,占污水处理成本的30%~40%。Municipal sludge is a by-product with a large amount of pollutants produced by sewage plants in the process of treating urban domestic sewage and industrial wastewater. From the appearance, municipal sludge is a black or dark brown semi-fluid or mud cake-like floc, which is a bacterial gel group formed by mud sand, fibers, animal and plant residues, and various microorganisms. It also contains copper, Arsenic, lead, zinc, chromium, cadmium and other heavy metals and refractory organic and inorganic pollutants. Its characteristics are: ① high water content, strong water holding capacity, difficult to compress and dehydrate; ② extremely poor stability, easy to deteriorate, and produce foul odor; ③ presents a floc state between fluid and colloid, poor fluidity; ④ contains many Simple treatment will cause heavy metal pollution; ⑤The output is large, and the treatment cost is high, accounting for 30% to 40% of the sewage treatment cost.

陶粒是以SiO2和Al2O3为主成分的原材料、经过高温焙烧而成的堆积密度小于1200kg/m3的多孔轻集料。具有密度小、强度高、吸水率低、保温、隔热、抗震及耐火等特点,近年来市场应用广泛,潜力巨大。可取代普通砂石配制轻集料混凝土,用作水处理滤料、吸附剂、透水路面材料,还可用作农业、园林中无土栽培的培养基以及桥面板、空心砌块等建材原料,目前已报导的污泥制陶粒的吸水率不足7%,孔隙率也较低,如何利用市政污泥协同炉渣制备出孔隙率在50%以上、吸水率在50%以上的多孔水处理陶粒现有技术中还尚未见报道。Ceramsite is a porous lightweight aggregate with a bulk density of less than 1200kg/m 3 , which is a raw material mainly composed of SiO 2 and Al 2 O 3 and fired at a high temperature. It has the characteristics of low density, high strength, low water absorption, heat preservation, heat insulation, earthquake resistance and fire resistance. It has been widely used in the market in recent years and has great potential. It can replace ordinary sand and gravel to prepare light aggregate concrete, which can be used as water treatment filter material, adsorbent, permeable pavement material, and can also be used as a medium for soilless cultivation in agriculture and gardens, as well as raw materials for building materials such as bridge decks and hollow blocks. The reported water absorption rate of sludge-made ceramsite is less than 7%, and the porosity is also low. How to use municipal sludge and slag to prepare porous water treatment ceramsite with a porosity of more than 50% and a water absorption rate of more than 50% Not yet reported in the prior art.

发明内容Contents of the invention

本发明的目的是,提供一种基于污泥的富孔高吸水率陶粒的制备方法,以市政污泥与生活垃圾炉渣为主要原料,添加玻璃粉来制备一种具有高吸水率和富孔的陶粒,可有效地解决现有城市污水处理厂污水污泥处理问题,有效地解决污水污泥的环境污染问题,拓展了污泥和炉渣的新用途。The object of the present invention is to provide a method for preparing sludge-based ceramsite with rich pores and high water absorption rate. Municipal sludge and domestic waste slag are used as main raw materials, and glass powder is added to prepare a ceramsite with high water absorption rate and rich pores. The ceramsite can effectively solve the problem of sewage sludge treatment in existing urban sewage treatment plants, effectively solve the environmental pollution problem of sewage sludge, and expand the new uses of sludge and slag.

本发明的核心创新点在于原料的选择,以生活垃圾焚烧炉渣与市政污泥为主,其中市政污泥中含有超过50%的有机物,根据这一特性,原料中不需要添加造孔剂,即可实现生活垃圾焚烧炉渣与市政污泥的资源化利用。本发明以污泥充当陶粒烧结过程中的发泡剂,污泥与炉渣协同作用,在预烧和焙烧机制下,添加玻璃粉使得在焙烧过程中产生足够多的液相,包裹产生的气体,将气体留在陶粒内部,形成更多的孔,最终使得陶粒具有更高的孔隙率和吸水率。The core innovation point of the present invention lies in the selection of raw materials, mainly domestic waste incineration slag and municipal sludge, wherein municipal sludge contains more than 50% organic matter, according to this characteristic, no pore-forming agent needs to be added to the raw materials, that is The resource utilization of domestic waste incineration slag and municipal sludge can be realized. In the present invention, sludge is used as a foaming agent in the sintering process of ceramsite, and the sludge and slag act synergistically. Under the mechanism of pre-firing and roasting, glass powder is added to generate enough liquid phase during the roasting process to wrap the generated gas. , leaving the gas inside the ceramsite, forming more pores, and finally making the ceramsite have higher porosity and water absorption.

为实现上述目的,本发明的技术方案是:For realizing the above object, technical scheme of the present invention is:

一种基于污泥的富孔高吸水率陶粒的制备方法,陶粒原材料中污泥含量为30~65wt%、垃圾焚烧炉渣5~40wt%、玻璃粉20~40wt%;陶粒焙烧前的原材料中主要成分及含量(参见表1)分别是:Al2O3含量为11~17wt%、SiO2含量为35~40wt%、MgO含量为2.5~3.5wt%、CaO含量为10~24wt%、K2O含量为1~2wt%、其余物质含量为5~10wt%。A method for preparing ceramsite with rich pores and high water absorption rate based on sludge. The sludge content in the ceramsite raw material is 30-65wt%, waste incineration slag is 5-40wt%, and glass powder is 20-40wt%. The ceramsite before roasting The main components and contents in the raw materials (see Table 1) are respectively: the content of Al2O3 is 11-17wt%, the content of SiO2 is 35-40wt%, the content of MgO is 2.5-3.5wt%, and the content of CaO is 10-24wt%. , the content of K 2 O is 1-2 wt%, and the content of other substances is 5-10 wt%.

制备方法的具体过程是:The concrete process of preparation method is:

S1:将污泥烘干至恒重;S1: drying the sludge to constant weight;

S2:将污泥与炉渣破碎球磨,并过200目筛;S2: Crushing and ball milling the sludge and slag, and passing through a 200-mesh sieve;

S3:按配比分别称取相应的污泥、炉渣、玻璃粉与淀粉,球磨混料;S3: Weigh the corresponding sludge, slag, glass powder and starch according to the proportion, and mix them by ball milling;

S4:在混匀的原料中加入40~60%的去离子水,陈腐;S4: add 40-60% deionized water to the mixed raw materials, stale;

S5:将陈腐之后的原料放入造粒机造粒,陶粒直径范围5~9mm;S5: Put the stale raw materials into the granulator to granulate, the diameter of ceramsite is 5-9mm;

S6:将搓好的陶粒放入烘箱中干燥;S6: Put the rubbed ceramsite into an oven to dry;

S7:将干燥之后的陶粒在马弗炉中焙烧,冷却之后取出;S7: roasting the dried ceramsite in a muffle furnace, and taking it out after cooling;

S8:陶粒性能测试。S8: Performance test of ceramsite.

优选地,所述市政污泥含量为55~65wt%、垃圾焚烧炉渣5~20wt%。Preferably, the municipal sludge content is 55-65 wt%, and the waste incineration slag is 5-20 wt%.

与现有技术相比,本发明的有益效果:Compared with prior art, the beneficial effect of the present invention:

本发明采用生活垃圾炉渣与污泥为主原料,并用玻璃粉为辅料来制备陶粒,不但工艺简单、成本低,还可使炉渣、污泥得到充分利用。在变废为宝的同时不仅节约了黏土、页岩等珍贵资源,同时还避免了炉渣、污泥的大量排放和堆积,降低了环境污染,真正达到了固体废物的资源化、无害化和减量化的目的,同时实现了变废为宝。从原料角度来说,由于污泥中含有大量有机物,在烧结过程中会产生大量气体,所以不需要使用发泡剂就能获得成孔效果极佳的陶粒。本发明的水处理陶粒吸水率能达到69.45%,孔隙率能够达到58.84%、比表面积大于3.8×104cm2/g,相较于其他的固废陶粒成孔效果更好,吸水率更高。The present invention adopts domestic waste slag and sludge as main raw materials, and uses glass powder as auxiliary material to prepare ceramsite, which not only has simple process and low cost, but also makes full use of slag and sludge. While turning waste into treasure, it not only saves precious resources such as clay and shale, but also avoids a large amount of discharge and accumulation of slag and sludge, reduces environmental pollution, and truly achieves the recycling, harmlessness and The purpose of reducing the amount is realized at the same time turning waste into wealth. From the perspective of raw materials, since the sludge contains a large amount of organic matter, a large amount of gas will be generated during the sintering process, so ceramsite with excellent pore-forming effect can be obtained without the use of foaming agents. The water treatment ceramsite of the present invention has a water absorption rate of 69.45%, a porosity of 58.84%, and a specific surface area greater than 3.8×10 4 cm 2 /g. Compared with other solid waste ceramsite, the pore-forming effect is better, and the water absorption rate higher.

本发明以污泥与生活垃圾焚烧炉渣为主要原料,添加适量玻璃粉,通过调控主要组分质量比为:SiO2/Al2O3=2.3~3.4,(SiO2+Al2O3)/(CaO+K2O+MgO)=1.7~3.8,来控制焙烧过程液相的生成量,从而提高陶粒的筒压强度,降低焙烧温度。将满足上述组分质量比的生活垃圾焚烧炉渣、污泥、玻璃粉和水混合均匀,经造粒、干燥后,在1000~1080℃温度下焙烧20~50min,即可得到性能优异的陶粒。而且陶粒表面粗糙、内部多孔,可用作水处理滤料,改性之后可以用来处理含油污水,如生活污水中的食用油、餐饮业的污水,含废油较高,能高效吸附油污。本发明具有工艺简单、生产成本低、资源利用率高、环境友好等诸多优点,不仅可同步实现污泥的彻底解毒和资源化高效利用,而且可为陶粒工业提供原料,减少对天然原料的依赖。The present invention uses sludge and domestic waste incineration slag as main raw materials, adds appropriate amount of glass powder, and adjusts the mass ratio of main components to be: SiO 2 /Al 2 O 3 =2.3-3.4, (SiO 2 +Al 2 O 3 )/ (CaO+K 2 O+MgO)=1.7~3.8, to control the amount of liquid phase generated in the roasting process, so as to increase the cylinder compressive strength of ceramsite and reduce the roasting temperature. Mix the domestic waste incineration slag, sludge, glass powder and water that satisfy the mass ratio of the above components evenly, granulate and dry, and then roast at 1000-1080°C for 20-50 minutes to obtain ceramsite with excellent properties . Moreover, the surface of ceramsite is rough and the interior is porous, so it can be used as a filter material for water treatment. After modification, it can be used to treat oily sewage, such as cooking oil in domestic sewage and sewage from the catering industry. It contains high waste oil and can efficiently absorb oil pollution. . The present invention has many advantages such as simple process, low production cost, high utilization rate of resources, and environmental friendliness. rely.

具体实施方式Detailed ways

为了使本领域技术人员更好地理解本申请中的技术方案,下面将结合实例对本申请中的技术方案进行清楚、完整的描述。In order to enable those skilled in the art to better understand the technical solutions in this application, the technical solutions in this application will be clearly and completely described below in conjunction with examples.

下述实例中涉及的原材料的化学组成见表1。The chemical compositions of the raw materials involved in the following examples are shown in Table 1.

表1:原材料化学组成(wt%)Table 1: Chemical Composition of Raw Materials (wt%)

化学组成chemical components SiO2 SiO 2 Al2O3 Al 2 O 3 MgOMgO CaOCaO K2OK 2 O 生活垃圾焚烧炉渣Domestic waste incineration slag 23.423.4 6.826.82 4.614.61 43.643.6 1.711.71 市政污泥municipal sludge 28.528.5 23.723.7 2.322.32 8.498.49 1.991.99 玻璃粉glass powder 67.967.9 5.075.07 3.503.50 10.210.2 0.070.07

实例一Example one

本实例一种基于污泥的富孔高吸水率陶粒的制备方法,原材料组成为市政污泥65%,垃圾焚烧炉渣5%,玻璃粉30%;This example is a preparation method of ceramsite with rich pores and high water absorption rate based on sludge. The raw materials are composed of 65% of municipal sludge, 5% of waste incineration slag, and 30% of glass powder;

包括以下步骤:Include the following steps:

S1:将污泥在烘箱中干燥至恒重,烘箱温度为80℃,烘干时间为12h;S1: Dry the sludge in an oven to constant weight, the oven temperature is 80°C, and the drying time is 12 hours;

S2:将烘干后的污泥与炉渣分别球磨成粉,过200目筛,球磨机转速为1500r/min,时间为30min;S2: Ball mill the dried sludge and slag into powder respectively, pass through a 200-mesh sieve, the speed of the ball mill is 1500r/min, and the time is 30min;

S3:按配方比例称取对应重量的原料,并球磨混匀,球磨机转速为800r/min,时间为5min;S3: Weigh the raw materials with the corresponding weight according to the formula ratio, and ball mill and mix them evenly. The speed of the ball mill is 800r/min, and the time is 5min;

S4:将混匀的原料倒入研磨锅中,加入50%的去离子水,混匀后陈腐20min;S4: Pour the mixed raw materials into a grinding pot, add 50% deionized water, mix and stale for 20 minutes;

S5:将陈腐之后的原料放入造粒机造粒,陶粒直径范围5~9mm;S5: Put the stale raw materials into the granulator to granulate, the diameter of ceramsite is 5-9mm;

S6:将成型的陶粒放入烘箱中烘干,烘箱温度80℃,时间3h;S6: put the formed ceramsite into an oven for drying, the oven temperature is 80°C, and the time is 3h;

S7:将烘干的陶粒放入马弗炉中进行焙烧,预热温度400℃,预热时间10min,升温速率5℃/min,焙烧温度1030℃,焙烧时间30min,升温速率10℃/min;然后等炉温自然冷却到室温时取出陶粒;S7: Put the dried ceramsite into the muffle furnace for roasting, the preheating temperature is 400°C, the preheating time is 10min, the heating rate is 5°C/min, the roasting temperature is 1030°C, the roasting time is 30min, and the heating rate is 10°C/min ; Then take out the ceramsite when the furnace temperature is naturally cooled to room temperature;

S8:对本实例中焙烧完成的陶粒进行性能测试,其中1h吸水率为69.45%,比表面积为3.79×104cm2/g,孔隙率58.84%,盐酸可溶率为0.7%,符合CJ/T 299—2008对水处理陶粒滤料的主要性能标准要求。另外重金属浸出浓度,可溶性氯含量、硫化物和硫酸盐含量及放射性均低于国家标准限值。S8: Perform a performance test on the fired ceramsite in this example. The 1h water absorption rate is 69.45%, the specific surface area is 3.79×10 4 cm 2 /g, the porosity is 58.84%, and the hydrochloric acid soluble rate is 0.7%, which conforms to CJ/ T 299-2008 Requirements for the main performance standards of ceramsite filter media for water treatment. In addition, the leaching concentration of heavy metals, soluble chlorine content, sulfide and sulfate content and radioactivity are all lower than the national standard limit.

实例二Example two

本实例一种基于污泥的富孔高吸水率陶粒的制备方法,原料组成为污泥55%,炉渣15%,玻璃粉30%;This example is a preparation method of ceramsite with rich pores and high water absorption rate based on sludge. The raw materials are composed of 55% sludge, 15% slag, and 30% glass powder;

包括以下步骤:Include the following steps:

S1:将污泥在烘箱中干燥至恒重,烘箱温度为80℃,烘干时间为12h;S1: Dry the sludge in an oven to constant weight, the oven temperature is 80°C, and the drying time is 12 hours;

S2:将烘干后的污泥与炉渣分别球磨成粉,过200目筛,球磨机转速为1500r/min,时间为30min;S2: Ball mill the dried sludge and slag into powder respectively, pass through a 200-mesh sieve, the speed of the ball mill is 1500r/min, and the time is 30min;

S3:按配方比例称取对应重量的原料,并球磨混匀,球磨机转速为800r/min,时间为5min;S3: Weigh the raw materials with the corresponding weight according to the formula ratio, and ball mill and mix them evenly. The speed of the ball mill is 800r/min, and the time is 5min;

S4:将混匀的原料倒入研磨锅中,加入50%的去离子水,混匀后陈腐2h;S4: Pour the mixed raw materials into a grinding pot, add 50% deionized water, mix and stale for 2 hours;

S5:将陈腐之后的原料放入造粒机造粒,陶粒直径范围5~9mm;S5: Put the stale raw materials into the granulator to granulate, the diameter of ceramsite is 5-9mm;

S6:将成型的陶粒放入烘箱中烘干,烘箱温度80℃,时间3h;S6: put the formed ceramsite into an oven for drying, the oven temperature is 80°C, and the time is 3h;

S7:将烘干的陶粒放入马弗炉中进行焙烧,预热温度400℃,预热时间10min,升温速率5℃/min,焙烧温度1050℃,焙烧时间30min,升温速率10℃/min;然后等炉温自然冷却到室温时取出陶粒;S7: Put the dried ceramsite into the muffle furnace for roasting, the preheating temperature is 400°C, the preheating time is 10min, the heating rate is 5°C/min, the roasting temperature is 1050°C, the roasting time is 30min, and the heating rate is 10°C/min ; Then take out the ceramsite when the furnace temperature is naturally cooled to room temperature;

S8:对本实例中焙烧完成的陶粒进行性能测试,其中吸水率为62.39%,比表面积为3.17×104cm2/g,孔隙率52.34%,盐酸可溶率为0.9%,符合CJ/T 299—2008对水处理陶粒滤料的主要性能标准要求。另外重金属浸出浓度,可溶性氯含量、硫化物和硫酸盐含量及放射性均低于国家标准限值。S8: Perform a performance test on the fired ceramsite in this example. The water absorption rate is 62.39%, the specific surface area is 3.17×10 4 cm 2 /g, the porosity is 52.34%, and the hydrochloric acid soluble rate is 0.9%, which conforms to CJ/T 299-2008 The main performance standard requirements for water treatment ceramsite filter media. In addition, the leaching concentration of heavy metals, soluble chlorine content, sulfide and sulfate content and radioactivity are all lower than the national standard limit.

实例三Example three

本实例一种基于污泥的富孔高吸水率陶粒的制备方法,原材料组成为市政污泥30%,垃圾焚烧炉渣40%,玻璃粉30%;This example is a preparation method of ceramsite with rich pores and high water absorption rate based on sludge. The raw materials are composed of 30% of municipal sludge, 40% of waste incineration slag, and 30% of glass powder;

包括以下步骤:Include the following steps:

S1:将污泥在烘箱中干燥至恒重,烘箱温度为80℃,烘干时间为12h;S1: Dry the sludge in an oven to constant weight, the oven temperature is 80°C, and the drying time is 12 hours;

S2:将烘干后的污泥与炉渣分别球磨成粉,过200目筛,球磨机转速为1500r/min,时间为30min;S2: Ball mill the dried sludge and slag into powder respectively, pass through a 200-mesh sieve, the speed of the ball mill is 1500r/min, and the time is 30min;

S3:按配方比例称取对应重量的原料,并球磨混匀,球磨机转速为800r/min,时间为5min;S3: Weigh the raw materials with the corresponding weight according to the formula ratio, and ball mill and mix them evenly. The speed of the ball mill is 800r/min, and the time is 5min;

S4:将混匀的原料倒入研磨锅中,加入50%的去离子水,混匀后陈腐20min;S4: Pour the mixed raw materials into a grinding pot, add 50% deionized water, mix and stale for 20 minutes;

S5:将陈腐之后的原料放入造粒机造粒,陶粒直径范围5~9mm;S5: Put the stale raw materials into the granulator to granulate, the diameter of ceramsite is 5-9mm;

S6:将成型的陶粒放入烘箱中烘干,烘箱温度80℃,时间3h;S6: put the formed ceramsite into an oven for drying, the oven temperature is 80°C, and the time is 3h;

S7:将烘干的陶粒放入马弗炉中进行焙烧,预热温度400℃,预热时间10min,升温速率5℃/min,焙烧温度1000℃,焙烧时间20min,升温速率10℃/min;然后等炉温自然冷却到室温时取出陶粒;S7: Put the dried ceramsite into the muffle furnace for roasting, the preheating temperature is 400°C, the preheating time is 10min, the heating rate is 5°C/min, the roasting temperature is 1000°C, the roasting time is 20min, and the heating rate is 10°C/min ; Then take out the ceramsite when the furnace temperature is naturally cooled to room temperature;

S8:对本实例中焙烧完成的陶粒进行性能测试,其中1h吸水率为50.34%,比表面积为2.53×104cm2/g,孔隙率51.13%,盐酸可溶率为1.1%,符合CJ/T 299—2008对水处理陶粒滤料的主要性能标准要求。另外重金属浸出浓度,可溶性氯含量、硫化物和硫酸盐含量及放射性均低于国家标准限值。S8: Perform a performance test on the fired ceramsite in this example. The 1h water absorption rate is 50.34%, the specific surface area is 2.53×10 4 cm 2 /g, the porosity is 51.13%, and the hydrochloric acid soluble rate is 1.1%, which conforms to CJ/ T 299-2008 Requirements for the main performance standards of ceramsite filter media for water treatment. In addition, the leaching concentration of heavy metals, soluble chlorine content, sulfide and sulfate content and radioactivity are all lower than the national standard limit.

对比例1Comparative example 1

本对比例在实例一基础上用钼尾矿替代垃圾焚烧炉渣,原材料组成为污泥65%,钼尾矿5%,玻璃粉30%。In this comparative example, on the basis of Example 1, molybdenum tailings are used to replace waste incineration slag, and the raw materials are composed of 65% of sludge, 5% of molybdenum tailings, and 30% of glass powder.

表2:原材料化学组成(wt%)Table 2: Chemical Composition of Raw Materials (wt%)

化学组成chemical components SiO2 SiO 2 Al2O3 Al 2 O 3 MgOMgO CaOCaO K2OK 2 O 钼尾矿Molybdenum tailings 68.868.8 14.314.3 0.6680.668 2.012.01 6.316.31

包括以下步骤:Include the following steps:

S1:将污泥在烘箱中干燥至恒重,烘箱温度为80℃,烘干时间为12h;S1: Dry the sludge in an oven to constant weight, the oven temperature is 80°C, and the drying time is 12 hours;

S2:将烘干后的污泥与钼尾矿分别球磨成粉,过200目筛,球磨机转速为1500r/min,时间为30min;S2: Ball mill the dried sludge and molybdenum tailings into powder respectively, pass through a 200-mesh sieve, and the speed of the ball mill is 1500r/min for 30 minutes;

S3:按配方比例称取对应重量的原料,并球磨混匀,球磨机转速为800r/min,时间为5min;S3: Weigh the raw materials with the corresponding weight according to the formula ratio, and ball mill and mix them evenly. The speed of the ball mill is 800r/min, and the time is 5min;

S4:将混匀的原料倒入研磨锅中,加入50%的去离子水,混匀后陈腐2h;S4: Pour the mixed raw materials into a grinding pot, add 50% deionized water, mix and stale for 2 hours;

S5:将陈腐之后的原料放入造粒机造粒,陶粒直径范围5~9mm;S5: Put the stale raw materials into the granulator to granulate, the diameter of ceramsite is 5-9mm;

S6:将成型的陶粒放入烘箱中烘干,烘箱温度80℃,时间3h;S6: put the formed ceramsite into an oven for drying, the oven temperature is 80°C, and the time is 3h;

S7:将烘干的陶粒放入马弗炉中进行焙烧,预热温度400℃,预热时间10min,升温速率5℃/min,焙烧温度1030℃,焙烧时间30min,升温速率10℃/min;然后等炉温自然冷却到室温时取出陶粒;S7: Put the dried ceramsite into the muffle furnace for roasting, the preheating temperature is 400°C, the preheating time is 10min, the heating rate is 5°C/min, the roasting temperature is 1030°C, the roasting time is 30min, and the heating rate is 10°C/min ; Then take out the ceramsite when the furnace temperature is naturally cooled to room temperature;

S8:对本实例中焙烧完成的陶粒进行性能测试,其中吸水率为36.71%,比表面积为1.97×104cm2/g,孔隙率41.23%,盐酸可溶率为1.2%。S8: Perform a performance test on the calcined ceramsite in this example. The water absorption is 36.71%, the specific surface area is 1.97×10 4 cm 2 /g, the porosity is 41.23%, and the hydrochloric acid solubility is 1.2%.

从上述测试结果可以看出,From the above test results, it can be seen that

对比例2Comparative example 2

本对比例在实例一基础上用凹凸棒石替代垃圾焚烧炉渣,原料组成为污泥65%,凹凸棒石5%,玻璃粉30%;This comparative example uses attapulgite to replace waste incineration slag on the basis of example one, and the raw material is composed of sludge 65%, attapulgite 5%, and glass powder 30%;

表3:原材料化学组成(wt%)Table 3: Chemical Composition of Raw Materials (wt%)

化学组成chemical components SiO2 SiO 2 Al2O3 Al 2 O 3 MgOMgO CaOCaO K2OK 2 O 凹凸棒石Attapulgite 63.663.6 15.215.2 4.514.51 5.495.49 1.71.7

包括以下步骤:Include the following steps:

S1:将污泥在烘箱中干燥至恒重,烘箱温度为80℃,烘干时间为12h;S1: Dry the sludge in an oven to constant weight, the oven temperature is 80°C, and the drying time is 12 hours;

S2:将烘干后的污泥与凹凸棒石分别球磨成粉,过200目筛,球磨机转速为1500r/min,时间为30min;S2: Ball mill the dried sludge and attapulgite into powder respectively, pass through a 200-mesh sieve, the speed of the ball mill is 1500r/min, and the time is 30min;

S3:按配方比例称取对应重量的原料,并球磨混匀,球磨机转速为800r/min,时间为5min;S3: Weigh the raw materials with the corresponding weight according to the formula ratio, and ball mill and mix them evenly. The speed of the ball mill is 800r/min, and the time is 5min;

S4:将混匀的原料倒入研磨锅中,加入50%的去离子水,混匀后陈腐2h;S4: Pour the mixed raw materials into a grinding pot, add 50% deionized water, mix and stale for 2 hours;

S5:将陈腐之后的原料放入造粒机造粒,陶粒直径范围5~9mm;S5: Put the stale raw materials into the granulator to granulate, the diameter of ceramsite is 5-9mm;

S6:将成型的陶粒放入烘箱中烘干,烘箱温度80℃,时间3h;S6: put the formed ceramsite into an oven for drying, the oven temperature is 80°C, and the time is 3h;

S7:将烘干的陶粒放入马弗炉中进行焙烧,预热温度400℃,预热时间10min,升温速率5℃/min,焙烧温度1030℃,焙烧时间30min,升温速率10℃/min;然后等炉温自然冷却到室温时取出陶粒;S7: Put the dried ceramsite into the muffle furnace for roasting, the preheating temperature is 400°C, the preheating time is 10min, the heating rate is 5°C/min, the roasting temperature is 1030°C, the roasting time is 30min, and the heating rate is 10°C/min ; Then take out the ceramsite when the furnace temperature is naturally cooled to room temperature;

S8:对本实例中焙烧完成的陶粒进行性能测试,其中吸水率为26.64%,比表面积为1.56×104cm2/g,孔隙率36.87%,盐酸可溶率为1.4%。S8: Perform a performance test on the calcined ceramsite in this example. The water absorption is 26.64%, the specific surface area is 1.56×10 4 cm 2 /g, the porosity is 36.87%, and the hydrochloric acid solubility is 1.4%.

本发明未述及之处适用于现有技术。What is not mentioned in the present invention is applicable to the prior art.

Claims (5)

1. A preparation method of a sludge-based porous high-water-absorption ceramsite is characterized by comprising the following steps: the municipal sludge and the household garbage incinerator slag are used as raw materials, glass powder is added, wherein the municipal sludge content is 55-65wt%, the household garbage incinerator slag content is 5-40wt% and the glass powder content is 20-40wt%, and the mass ratio of the main components is regulated and controlled to be: siO (SiO) 2 /Al 2 O 3 =2.3~3.4,(SiO 2 +Al 2 O 3 )/(CaO+K 2 O+mgo) =1.7 to 3.8 to control the amount of liquid phase produced during the firing, thereby increasing the cylinder pressure of the ceramic grains and reducing the firing temperature; uniformly mixing household garbage incinerator slag, municipal sludge, glass powder and water which meet the mass ratio of the components, granulating, drying, and roasting at 1000-1080 ℃ for 20-50 min to obtain porous water treatment ceramsite with the porosity of more than 50% and the water absorption rate of more than 50%;
the porous water treatment ceramsite has a water absorption rate of 51.34-69.45% and a specific surface area of 2.4-3.8X10 after 1h 4 cm 2 The porosity is 51.13-58.84%, the hydrochloric acid solubility is 0.7-1.1%, and the heavy metal leaching concentration, the soluble chlorine content, the sulfide and sulfate content and the radioactivity in the ceramsite are all lower than the national standard limit;
the chemical composition of the raw materials is as follows:
Figure QLYQS_1
2. the method of manufacturing according to claim 1, characterized in that: municipal sludge and household garbage incinerator slag are used as raw materials, and auxiliary material glass powder is added; the main components and the contents of the raw materials before the ceramic grain roasting are respectively as follows: al (Al) 2 O 3 The content is 11-17 wt percent, siO 2 35 to 40 weight percent of MgO, 2.5 to 3.5 weight percent of CaO, 10 to 24 weight percent of CaO and K 2 The content of O is 1-2 wt% and the content of the rest substances is 5-10 wt%.
3. A preparation method of a sludge-based porous high-water-absorption ceramsite is characterized by comprising the following steps: the municipal sludge content in the ceramsite raw material is 55-65wt%, the garbage incinerator slag is 5-40wt% and the glass powder is 20-40wt%; the main components and the contents of the raw materials before the ceramic grain roasting are respectively as follows: al (Al) 2 O 3 The content is 11-17 wt percent, siO 2 35 to 40 weight percent of MgO, 2.5 to 3.5 weight percent of CaO, 10 to 24 weight percent of CaO and K 2 The O content is 1-2 wt%, and the content of the rest substances is 5-10 wt%; the municipal sludge contains more than 50% of organic matters;
the preparation method comprises the following specific processes:
s1: drying municipal sludge to constant weight;
s2: crushing and ball milling municipal sludge and slag, and sieving with a 200-mesh sieve;
s3: respectively weighing corresponding municipal sludge, slag, glass powder and starch according to a proportion, and ball-milling and mixing;
s4: adding 40-60% deionized water into the uniformly mixed raw materials, and aging;
s5: granulating the raw materials after ageing in a granulator, wherein the diameter of the ceramsite ranges from 5 mm to 9mm;
s6: putting the rubbed haydite into a baking oven for drying;
s7: roasting the dried ceramsite in a muffle furnace at a preheating temperature of 400 ℃ for 10min and a heating rate of 5 ℃/min, wherein the roasting temperature is 1000-1080 ℃; roasting time is 20-50 min, and heating rate is 10 ℃/min; then taking out the ceramsite when the furnace temperature is naturally cooled to room temperature;
the chemical composition of the raw materials is as follows:
Figure QLYQS_2
4. a method of preparation according to claim 3, characterized in that: the municipal sludge content is 55-65wt% and the garbage incinerator slag content is 5-20wt%.
5. A ceramsite, characterized in that it is obtained by the method according to any one of claims 1 to 4.
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