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CN114790107A - A method for preparing SiO2-Si3N4 composite ceramics at low temperature by using polysilicon cutting waste - Google Patents

A method for preparing SiO2-Si3N4 composite ceramics at low temperature by using polysilicon cutting waste Download PDF

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CN114790107A
CN114790107A CN202210466287.1A CN202210466287A CN114790107A CN 114790107 A CN114790107 A CN 114790107A CN 202210466287 A CN202210466287 A CN 202210466287A CN 114790107 A CN114790107 A CN 114790107A
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李军成
王蓉
邱锋
李果轩
梁金山
高新泽
魏信霖
管东
钟艺
郭长庆
王睿宁
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Abstract

The invention belongs to the technical field of metallurgical resource recycling, and discloses a method for preparing SiO by using polycrystalline silicon cutting waste at low temperature 2 ‑Si 3 N 4 A method for compounding ceramics. Processing the polycrystalline silicon cutting waste to the standard of laboratory use, mixing the polycrystalline silicon cutting waste with a diluent, uniformly ball-milling, and controlling a nitriding reaction by reasonably selecting a nitriding atmosphere to obtain a nitriding product; crushing and grinding the nitriding product, and adding SiO 2 C, sintering aid, ball milling and mixing, and cold isostatic pressing to prepare a sample before ammoniation; through reasonable selection of ammoniation atmosphere and control of ammoniation reaction, SiO is obtained 2 ‑Si 3 N 4 Composite ceramics. The invention has the advantages that the by-product generation is avoided by controlling the powder composition and ammoniation conditions, and SiO is utilized 2 The volume effect is effectively reduced by the carbothermic reduction reaction of the C and the C, and finally the SiO with uniform components and good performance is obtained 2 ‑Si 3 N 4 The composite ceramic realizes the resource utilization of the photovoltaic industrial chain waste and the economic development of the ceramic industrial chain.

Description

一种利用多晶硅切割废料在低温下制备SiO2-Si3N4复合陶瓷 的方法A method for preparing SiO2-Si3N4 composite ceramics at low temperature by using polysilicon cutting waste

技术领域technical field

本发明属于冶金资源循环利用技术领域,涉及一种利用多晶硅切割废料在低温下制备SiO2-Si3N4复合陶瓷的方法。The invention belongs to the technical field of metallurgical resource recycling, and relates to a method for preparing SiO 2 -Si 3 N 4 composite ceramics at low temperature by using polysilicon cutting waste.

背景技术Background technique

多晶硅切割废料是光伏产业快速发展所带来的硅基固废产物之一,年产量约为200千吨。从废料中回收单质硅产品存在难度大、成本高、杂质含量高等问题,使得大量废料堆积,不仅占用了大量土地资源,并且一定程度上造成了资源浪费和环境污染。Polysilicon cutting waste is one of the silicon-based solid waste products brought about by the rapid development of the photovoltaic industry, with an annual output of about 200 kilotons. Recycling elemental silicon products from waste has the problems of difficulty, high cost and high impurity content, which makes a large amount of waste accumulate, which not only occupies a lot of land resources, but also causes resource waste and environmental pollution to a certain extent.

相比从多晶硅切割废料中回收利用单质硅产品,将废料直接转化为有高附加值资源如硅基陶瓷,省去提纯硅粉的必要步骤,不仅简化了工艺流程,降低了陶瓷的原料成本,而且促进了更高附加值产物的生产。Si3N4陶瓷便是其高附加值产物的代表之一,其具备的高强度、耐腐蚀使其在机械、制造业得到广泛应用,但受限于高介电常数和介电损耗,其在航天行业的发展受到限制。SiO2-Si3N4复合陶瓷的出现则解决了这一问题,它不仅具备了Si3N4的高强度、耐腐蚀,同时还具备了SiO2的低介电常数和介电损耗,是制备航天天线窗等的优质材料。然而在制备SiO2-Si3N4复合陶瓷过程中,如果简单的是将硅粉、二氧化硅等混合烧结,则由于氧含量、颗粒粗糙度等因素的影响,得到的产物中必然会产生氮氧化硅等副产物,对陶瓷产品的介电性能、力学性能有极大的影响,难以在实际方面应用。因此,如何合理避免氮氧化硅等副产物的生成是其制备成优良SiO2-Si3N4复合陶瓷的前提。Compared with the recycling of elemental silicon products from polysilicon cutting waste, the waste is directly converted into high value-added resources such as silicon-based ceramics, eliminating the necessary steps of purifying silicon powder, which not only simplifies the process flow, but also reduces the raw material cost of ceramics. And it promotes the production of higher value-added products. Si 3 N 4 ceramics is one of the representatives of its high value-added products. Its high strength and corrosion resistance make it widely used in machinery and manufacturing, but it is limited by high dielectric constant and dielectric loss. Development in the aerospace industry is limited. The emergence of SiO 2 -Si 3 N 4 composite ceramics solves this problem. It not only has the high strength and corrosion resistance of Si 3 N 4 , but also has the low dielectric constant and dielectric loss of SiO 2 . High-quality materials for the preparation of aerospace antenna windows, etc. However, in the process of preparing SiO 2 -Si 3 N 4 composite ceramics, if it is simply to mix and sinter silicon powder, silicon dioxide, etc., due to the influence of oxygen content, particle roughness and other factors, the resulting product will inevitably produce By-products such as silicon oxynitride have a great influence on the dielectric properties and mechanical properties of ceramic products, and are difficult to apply in practice. Therefore, how to reasonably avoid the formation of by-products such as silicon oxynitride is the premise for the preparation of excellent SiO 2 -Si 3 N 4 composite ceramics.

由于氮氧化硅具备高温分解的特性,目前现有的技术通常采用提高烧结温度并同步增加高温区间的保温时长,以此来消除副产物,即先生成副产物,再分解副产物。但是这些控制技术通常建立在高温、长时效、高损耗的基础之上,带来的实际经济效益并不高。若想要降低高温烧结,减少耗能,常规的控制方法是添加一定比例的烧结助剂,使其在体系中随着烧结过程形成多元共熔体,可以在一定程度上降低烧结温度。但与此同时,部分多元共熔体的形成也会带来高达30%甚至更甚的体积效应,使该控制方法的实际收益并不高。因此,有必要开发新的能够在低温下制备出复合陶瓷的方法。Since silicon oxynitride has the characteristics of high temperature decomposition, the current technology usually adopts increasing the sintering temperature and simultaneously increasing the holding time in the high temperature range, so as to eliminate by-products, that is, by-products are generated first, and then by-products are decomposed. However, these control technologies are usually based on high temperature, long aging and high loss, and the actual economic benefits brought are not high. If you want to reduce high temperature sintering and reduce energy consumption, the conventional control method is to add a certain proportion of sintering aids to form a multi-component eutectic in the system with the sintering process, which can reduce the sintering temperature to a certain extent. But at the same time, the formation of part of the multicomponent eutectic will also bring up to 30% or even more volume effect, so that the actual benefit of this control method is not high. Therefore, it is necessary to develop new methods to prepare composite ceramics at low temperature.

发明内容SUMMARY OF THE INVENTION

Si、SiO2混合粉体在传统的陶瓷制备工艺中难以生成SiO2-Si3N4复合陶瓷,易于生成氮氧化硅等副产物。针对易于产生副产物的难题,本发明的目的在于:提供一种利用多晶硅切割废料在低温下制备SiO2-Si3N4复合陶瓷的方法,通过控制粉体组成和氨化条件有效规避氮氧化硅等副产物的生成,利用SiO2和C发生的碳热还原反应有效降低体积效应,最终得到成分均一、性能良好的SiO2-Si3N4复合陶瓷,从而实现了光伏产业链废弃物的资源化利用和陶瓷产业链的经济发展。Si and SiO 2 mixed powder is difficult to generate SiO 2 -Si 3 N 4 composite ceramics in the traditional ceramic preparation process, and it is easy to generate by-products such as silicon oxynitride. Aiming at the problem that by-products are easily generated, the purpose of the present invention is to provide a method for preparing SiO 2 -Si 3 N 4 composite ceramics at low temperature by using polysilicon cutting waste, which can effectively avoid nitrogen oxidation by controlling the powder composition and ammoniation conditions The generation of by-products such as silicon can effectively reduce the volume effect by the carbothermic reduction reaction of SiO 2 and C, and finally obtain SiO 2 -Si 3 N 4 composite ceramics with uniform composition and good performance, thus realizing the elimination of waste in the photovoltaic industry chain. Resource utilization and economic development of the ceramic industry chain.

本发明提供了一种通过多晶硅切割废料氮化+氨化烧制陶瓷来制备复合陶瓷的思路,以此实现多晶硅切割废料在低温下制备SiO2-Si3N4复合陶瓷的方法,包括以下步骤:The invention provides an idea of preparing composite ceramics by nitriding and ammoniating sintering ceramics from polysilicon cutting wastes, so as to realize the method for preparing SiO2 - Si3N4 composite ceramics from polysilicon cutting wastes at low temperature, comprising the following steps :

(1)多晶硅切割废料的纯化处理:(1) Purification of polysilicon cutting waste:

多晶硅切割废料经烘干、粉碎、冲洗杂质、再次烘干、研磨、过筛得到粉体,即为纯化后的多晶硅切割废料,其中Si纯度为2N级别;The polysilicon cutting waste is dried, pulverized, washed with impurities, dried again, ground and sieved to obtain powder, which is the purified polysilicon cutting waste, wherein the Si purity is 2N;

(2)多晶硅切割废料的氮化处理(2) Nitriding treatment of polysilicon cutting waste

在步骤(1)得到纯化后的多晶硅切割废料中加入稀释剂,球磨混合后,进行气氛氮化,氮化反应后得到氮化产物;A diluent is added to the purified polysilicon cutting waste obtained in step (1), and after ball milling and mixing, atmosphere nitriding is performed, and a nitriding product is obtained after nitriding reaction;

所述稀释剂为α-Si3N4或β-Si3N4,添加量不超过纯化后的多晶硅切割废料质量的20%。The diluent is α-Si 3 N 4 or β-Si 3 N 4 , and the added amount does not exceed 20% of the mass of the purified polysilicon cutting waste.

所述氮化反应中,氮化气体为氮气或氮氢混合气中的一种,其中,氮氢混合气中,氮气和氢气的体积比在75:25-95:5之间。In the nitriding reaction, the nitriding gas is one of nitrogen gas or nitrogen-hydrogen mixed gas, wherein, in the nitrogen-hydrogen mixed gas, the volume ratio of nitrogen and hydrogen is between 75:25-95:5.

所述氮化反应中,氮化设备采用程序控温的气氛管式炉,确保炉内温度以1-5℃/min的速度升温至1200-1450℃,然后恒温0.5-2.5h。该升温制度有利于氮化反应的进行。In the nitriding reaction, the nitriding equipment adopts a temperature-controlled atmosphere tube furnace to ensure that the temperature in the furnace is raised to 1200-1450°C at a rate of 1-5°C/min, and then the temperature is kept constant for 0.5-2.5h. The temperature rise system is favorable for the nitridation reaction to proceed.

氮化气氛和稀释剂的使用,能够促进氮化反应的进行。The use of nitriding atmosphere and diluent can promote the nitriding reaction.

(3)SiO2-Si3N4复合陶瓷的氨化烧制(3) Ammonia firing of SiO 2 -Si 3 N 4 composite ceramics

将步骤(2)中的氮化产物用研钵研磨至300目以下,添加一定比例的SiO2、C、烧结助剂,球磨至物料混匀,烘干物料,冷等静压成型得到氨化前样品。在气氛管式炉设备中通入氨化气体后,以1-5℃/min的速度升温至1100-1450℃,然后恒温1-3h,再以1-5℃/min的速度降温至室温,得到SiO2-Si3N4复合陶瓷。该热处理制度可以促进碳热还原反应的进行,有利于降低多元玻璃相共熔体带来的体积效应,从而提升陶瓷烧结体的性能。Grinding the nitrided product in step (2) to below 300 mesh with a mortar, adding a certain proportion of SiO 2 , C and sintering aids, ball milling until the material is mixed, drying the material, and cold isostatic pressing to obtain ammoniated previous sample. After the ammoniated gas is introduced into the atmosphere tube furnace equipment, the temperature is raised to 1100-1450°C at a rate of 1-5°C/min, then kept at a constant temperature for 1-3 hours, and then cooled to room temperature at a rate of 1-5°C/min. The SiO 2 -Si 3 N 4 composite ceramic was obtained. The heat treatment system can promote the carbothermic reduction reaction, which is beneficial to reduce the volume effect brought by the multi-glass phase eutectic, thereby improving the performance of the ceramic sintered body.

所述烧结助剂为MgO、Al2O3、Y2O3中的一种或几种,烧结助剂能够降低氨化过程烧结温度;添加SiO2、C进行碳热还原反应,能够降低氨化过程带来的体积效应。The sintering aid is one or more of MgO, Al 2 O 3 , and Y 2 O 3 , and the sintering aid can reduce the sintering temperature in the ammoniation process; adding SiO 2 and C to carry out a carbothermal reduction reaction can reduce ammonia volume effect brought about by the process.

所述的SiO2、C、烧结助剂添加量分别不超过氮化产物质量的100%、20%、20%。The added amounts of SiO 2 , C and sintering aids do not exceed 100%, 20%, and 20% of the quality of the nitrided product, respectively.

所述的氨化气体为氨气、氮氨混合气、氢氨混合气及氮氢氨混合气中的一种,其中,使用混合气时,氨气的体积占比控制在50%以上。The ammoniated gas is one of ammonia gas, nitrogen-ammonia mixed gas, hydrogen-ammonia mixed gas and nitrogen-hydrogen-ammonium mixed gas, wherein, when the mixed gas is used, the volume ratio of ammonia gas is controlled to be more than 50%.

本发明的有益效果为:The beneficial effects of the present invention are:

(1)加入的原料主体为多晶硅切割废料。陶瓷原料成本低,同时解决了废料堆放带来的环境污染,促进了高附加值产品产业链的形成。(1) The main body of the added raw material is polysilicon cutting waste. The cost of ceramic raw materials is low, and at the same time, it solves the environmental pollution caused by waste stacking, and promotes the formation of an industrial chain of high value-added products.

(2)氮化过程中使用的氮化气氛为氮气、氮氢混合气中的一种气体,氢气能够破除硅表面的天然氧化层膜,有效促进氮化反应的进行。(2) The nitriding atmosphere used in the nitriding process is a gas in nitrogen and nitrogen-hydrogen mixture. Hydrogen can break the natural oxide film on the silicon surface and effectively promote the nitriding reaction.

(3)氮化过程中加入的稀释剂为α-Si3N4或β-Si3N4,总量按不超过纯化后的多晶硅切割废料总重量的20%进行控制。稀释剂的添加能够作为反应晶种,促进氮化反应的进行。(3) The diluent added in the nitriding process is α-Si 3 N 4 or β-Si 3 N 4 , and the total amount is controlled so as not to exceed 20% of the total weight of the purified polysilicon cutting waste. The addition of the diluent can act as a reaction seed to promote the progress of the nitridation reaction.

(4)氨化过程中加入的烧结助剂为MgO、Al2O3及Y2O3中的一种或几种,总量按不超过氮化产物总重量的20%进行控制。烧结助剂的添加能够生成多元玻璃相共熔体,有效降低陶瓷烧结体烧结温度。(4) The sintering aids added in the ammoniation process are one or more of MgO, Al 2 O 3 and Y 2 O 3 , and the total amount is controlled not to exceed 20% of the total weight of the nitrided product. The addition of sintering aids can generate a multi-glass phase eutectic, which can effectively reduce the sintering temperature of the ceramic sintered body.

(5)氨化过程中加入SiO2、C,总量按不超过氮化产物总重量的100%、20%进行控制。碳热还原反应的总反应式为:3SiO2+6C+4NH3→Si3N4+6CO+6H2,能有效降低烧结助剂在烧结过程中形成的低共熔体带来的体积效应,减少陶瓷的线收缩率,从而提高陶瓷的力学性能。(5) SiO 2 and C are added in the ammoniation process, and the total amount is controlled so as not to exceed 100% and 20% of the total weight of the nitrided product. The overall reaction formula of the carbothermic reduction reaction is: 3SiO 2 +6C+4NH 3 →Si 3 N 4 +6CO+6H 2 , which can effectively reduce the volume effect of the eutectic formed by the sintering aid during the sintering process. Reduce the linear shrinkage of ceramics, thereby improving the mechanical properties of ceramics.

(6)氨化过程中使用的氨化气氛为氨气、氮氨混合气、氢氨混合气及氮氢氨混合气中的一种。使用混合气时,氨气占总气体50%以上,氨化气体能够有效的降低陶瓷烧结体烧结温度,减少副产物的生成。(6) The ammoniated atmosphere used in the ammoniation process is one of ammonia, nitrogen-ammonia mixture, hydrogen-ammonia mixture and nitrogen-hydrogen-ammonia mixture. When the mixed gas is used, the ammonia gas accounts for more than 50% of the total gas, and the ammoniated gas can effectively reduce the sintering temperature of the ceramic sintered body and reduce the generation of by-products.

附图说明Description of drawings

图1为本发明提供的利用多晶硅切割废料在低温下制备SiO2-Si3N4复合陶瓷的方法的工艺流程图。FIG. 1 is a process flow diagram of a method for preparing SiO 2 -Si 3 N 4 composite ceramics at low temperature by using polysilicon cutting waste provided by the present invention.

图2实施案例XRD结果。Figure 2 Example XRD results.

具体实施方式Detailed ways

下面结合具体实施方式和数据对本发明内容及效果作进一步说明。The content and effects of the present invention will be further described below in conjunction with specific embodiments and data.

实施例1:Example 1:

取某太阳能电池板公司线切割阶段的多晶硅切割废料,成分主要包括Si、SiO2及少量金属氧化物杂质,纯化处理后Si的纯度在99%以上,向其中加入稀释剂α-Si3N4,加入量为纯化后的多晶硅切割废料质量的20%;选择氮氢(95:5)混合气作为氮化气氛;加入MgO和Y2O3作为烧结助剂,加入量为总质量的7%;选择氮氨(4:6)混合气作为氨化气氛。Take the polysilicon cutting waste in the wire cutting stage of a solar panel company. The components mainly include Si, SiO 2 and a small amount of metal oxide impurities. The purity of Si after purification treatment is above 99%, and diluent α-Si 3 N 4 is added to it. , the addition amount is 20% of the mass of the purified polysilicon cutting waste; the nitrogen-hydrogen (95:5) mixture is selected as the nitriding atmosphere; MgO and Y 2 O 3 are added as sintering aids, and the addition amount is 7% of the total mass ; Select nitrogen-ammonia (4:6) gas mixture as ammoniation atmosphere.

为了对本发明内容和效果做进一步验证,实施时包括以下具体的工艺步骤:In order to further verify the content and effect of the present invention, the following specific process steps are included during implementation:

(1)将纯化处理后的多晶硅切割废料和稀释剂同时装入球磨罐,混合均匀后置于氧化铝坩埚中,在氮化气氛下升温至1400℃并保温2h,随炉冷却至室温得到氮化产物;(1) Put the purified polysilicon cutting waste and diluent into a ball mill jar at the same time, mix them evenly, and place them in an alumina crucible. In a nitriding atmosphere, the temperature is raised to 1400 ° C and kept for 2 hours, and then cooled to room temperature with the furnace to obtain nitrogen. chemical product;

(2)将步骤(1)氮化产物破碎研磨后,加入烧结助剂、SiO2、C,再次球磨混匀后,冷等静压成型并置于石墨坩埚中,实施例1氨化前样品成分如表1所示;(2) After crushing and grinding the nitrided product in step (1), add sintering aids, SiO 2 , and C, and after ball milling and mixing again, cold isostatic pressing is formed and placed in a graphite crucible. Example 1 Sample before ammoniation The ingredients are shown in Table 1;

表1实施例1氨化前样品成分Table 1 Example 1 Sample composition before ammoniation

Figure BDA0003624300570000041
Figure BDA0003624300570000041

(3)在氨化气氛下升温至1350℃并保温2.5h,随炉冷却至室温得到SiO2-Si3N4复合陶瓷。对所得的复合陶瓷进行性能测试。(3) The temperature is raised to 1350° C. in an ammoniated atmosphere and kept for 2.5 hours, and then cooled to room temperature with the furnace to obtain SiO 2 -Si 3 N 4 composite ceramics. The properties of the obtained composite ceramics were tested.

实施例2:Example 2:

取某太阳能电池板公司线切割阶段的多晶硅切割废料,成分主要包括Si、SiO2及少量金属氧化物杂质,纯化处理后Si的纯度在99%以上,向其中加入稀释剂β-Si3N4,加入量为纯化后的多晶硅切割废料质量的10%;选择氮氢(9:1)混合气作为氮化气氛;加入MgO作为烧结助剂,加入量为总质量的8%;选择氮氢氨(30:10:60)混合气作为氨化气氛。Take the polysilicon cutting waste from the wire cutting stage of a solar panel company. The components mainly include Si, SiO 2 and a small amount of metal oxide impurities. The purity of Si after purification treatment is above 99%, and the diluent β-Si 3 N 4 is added to it. , the addition amount is 10% of the mass of the purified polysilicon cutting waste; nitrogen-hydrogen (9:1) mixture is selected as the nitriding atmosphere; MgO is added as a sintering aid, and the addition amount is 8% of the total mass; nitrogen-hydrogen ammonia is selected (30:10:60) mixed gas was used as ammoniation atmosphere.

为了对本发明内容和效果做进一步验证,实施时包括以下具体的工艺步骤:In order to further verify the content and effect of the present invention, the following specific process steps are included during implementation:

(1)将纯化处理后的多晶硅切割废料和稀释剂同时装入球磨罐,混合均匀后置于氧化铝坩埚中,在氮化气氛下升温至1300℃并保温2h,随炉冷却至室温得到氮化产物;(1) Put the purified polysilicon cutting waste and diluent into a ball mill jar at the same time, mix them evenly, and place them in an alumina crucible. In a nitriding atmosphere, the temperature is raised to 1300 ° C and kept for 2 hours, and then cooled to room temperature with the furnace to obtain nitrogen. chemical product;

(2)将步骤(1)的氮化产物破碎研磨后,加入烧结助剂、SiO2、C,再次球磨混匀后,冷等静压成型并置于石墨坩埚中,实施例2氨化前样品成分如表2所示;(2) After crushing and grinding the nitrided product of step (1), add sintering aids, SiO 2 , C, and after ball milling and mixing again, cold isostatic pressing molding and placing in a graphite crucible, Example 2 before ammoniation The sample composition is shown in Table 2;

表2实施例2氨化前样品成分Table 2 Example 2 Sample composition before ammoniation

Figure BDA0003624300570000042
Figure BDA0003624300570000042

(3)在氨化气氛下升温至1300℃并保温1.5h,随炉冷却至室温得到SiO2-Si3N4复合陶瓷。对所得的复合陶瓷进行性能测试。(3) The temperature is raised to 1300° C. in an ammoniated atmosphere and kept for 1.5 hours, and then cooled to room temperature with the furnace to obtain SiO 2 -Si 3 N 4 composite ceramics. The properties of the obtained composite ceramics were tested.

实施例3:Example 3:

取某太阳能电池板公司线切割阶段的多晶硅切割废料,成分主要包括Si、SiO2及少量金属氧化物杂质,纯化处理后Si的纯度在99%以上,向其中加入稀释剂α-Si3N4,加入量为纯化后的多晶硅切割废料质量的10%;选择高纯氮气作为氮化气氛;加入MgO和Al2O3作为烧结助剂,加入量为总质量的8%;选择氨气作为氨化气氛。Take the polysilicon cutting waste in the wire cutting stage of a solar panel company. The components mainly include Si, SiO 2 and a small amount of metal oxide impurities. The purity of Si after purification treatment is above 99%, and diluent α-Si 3 N 4 is added to it. , the addition amount is 10% of the mass of the purified polysilicon cutting waste; high-purity nitrogen is selected as the nitriding atmosphere; MgO and Al 2 O 3 are added as sintering aids, and the addition amount is 8% of the total mass; ammonia gas is selected as the ammonia atmosphere.

为了对本发明内容和效果做进一步验证,实施时包括以下具体的工艺步骤:In order to further verify the content and effect of the present invention, the following specific process steps are included during implementation:

(1)将纯化处理后的多晶硅切割废料和稀释剂同时装入球磨罐,混合均匀后置于氧化铝坩埚中,在氮化气氛下升温至1400℃并保温2h,随炉冷却至室温得到氮化产物;(1) Put the purified polysilicon cutting waste and diluent into a ball mill jar at the same time, mix them evenly, and place them in an alumina crucible. In a nitriding atmosphere, the temperature is raised to 1400 ° C and kept for 2 hours, and then cooled to room temperature with the furnace to obtain nitrogen. chemical product;

(2)将步骤(1)的氮化产物破碎研磨后,加入烧结助剂、SiO2、C,再次球磨混匀后,冷等静压成型并置于石墨坩埚中,实施案例3氨化前样品成分如表3所示;(2) After crushing and grinding the nitrided product in step (1), adding sintering aids, SiO 2 , C, and ball-milling and mixing again, cold isostatic pressing and placing in a graphite crucible. Example 3 Before ammoniation The sample composition is shown in Table 3;

表3实施例3氨化前样品成分Table 3 Example 3 Sample composition before ammoniation

Figure BDA0003624300570000051
Figure BDA0003624300570000051

(3)在氨化气氛下升温至1400℃并保温2h,随炉冷却至室温得到SiO2-Si3N4复合陶瓷。对所得的复合陶瓷进行性能测试。(3) The temperature is raised to 1400° C. and kept for 2 hours in an ammoniated atmosphere, and then cooled to room temperature with the furnace to obtain SiO 2 -Si 3 N 4 composite ceramics. The properties of the obtained composite ceramics were tested.

实施例4:Example 4:

取某太阳能电池板公司线切割阶段的多晶硅切割废料,成分主要包括Si、SiO2及少量金属氧化物杂质,纯化处理后Si的纯度在99%以上,向其中加入稀释剂β-Si3N4,加入量为纯化后的多晶硅切割废料质量的10%;选择高纯氮气作为氮化气氛;加入Al2O3和Y2O3作为烧结助剂,加入量为总质量的6%;选择氢氨(5:95)混合气作为氨化气氛。Take the polysilicon cutting waste from the wire cutting stage of a solar panel company. The components mainly include Si, SiO 2 and a small amount of metal oxide impurities. The purity of Si after purification treatment is above 99%, and the diluent β-Si 3 N 4 is added to it. , the addition amount is 10% of the mass of the purified polysilicon cutting waste; high-purity nitrogen is selected as the nitriding atmosphere; Al 2 O 3 and Y 2 O 3 are added as sintering aids, and the addition amount is 6% of the total mass; hydrogen is selected Ammonia (5:95) gas mixture was used as the ammoniation atmosphere.

为了对本发明内容和效果做进一步验证,实施时包括以下具体的工艺步骤:In order to further verify the content and effect of the present invention, the following specific process steps are included during implementation:

(1)将研磨清洗后的多晶硅切割废料和稀释剂同时装入球磨罐,保证废料与稀释剂混合均匀后置于氧化铝坩埚中,在氮化气氛下,在氮化气氛下升温至1450℃并保温2h,随炉冷却至室温得到氮化产物;(1) The polysilicon cutting waste and the diluent after grinding and cleaning are loaded into the ball mill jar at the same time to ensure that the waste and the diluent are mixed evenly and then placed in an alumina crucible. Under the nitriding atmosphere, the temperature is raised to 1450 ℃ And kept for 2h, cooled to room temperature with the furnace to obtain the nitrided product;

(2)将步骤(1)的氮化产物破碎研磨后,加入烧结助剂、SiO2、C,再次球磨混匀后,冷等静压成型并置于石墨坩埚中,实施例4氨化前样品成分如表4所示;(2) After crushing and grinding the nitrided product of step (1), add sintering aids, SiO 2 , C, and after ball milling and mixing again, cold isostatic pressing molding and placing in a graphite crucible, Example 4 before ammoniation The sample composition is shown in Table 4;

表4实施例4氨化前样品成分Table 4 Example 4 Sample composition before ammoniation

Figure BDA0003624300570000052
Figure BDA0003624300570000052

Figure BDA0003624300570000061
Figure BDA0003624300570000061

(3)在氨化气氛下升温至1350℃并保温2h,随炉冷却至室温得到SiO2-Si3N4复合陶瓷。对所得的复合陶瓷进行性能测试。(3) The temperature is raised to 1350° C. and kept for 2 hours in an ammoniated atmosphere, and then cooled to room temperature with the furnace to obtain SiO 2 -Si 3 N 4 composite ceramics. The properties of the obtained composite ceramics were tested.

利用X射线衍射(XRD)对实施例1、2、3、4中的复合陶瓷进行扫描分析,结果如图2所示。The composite ceramics in Examples 1, 2, 3, and 4 were scanned and analyzed by X-ray diffraction (XRD), and the results are shown in FIG. 2 .

对实施例1、2、3、4中的复合陶瓷进行性能测试,结果如表5所示。The composite ceramics in Examples 1, 2, 3, and 4 were tested for performance, and the results are shown in Table 5.

表5复合陶瓷性能测试结果Table 5 Performance test results of composite ceramics

实施例1Example 1 实施例2Example 2 实施例3Example 3 实施例4Example 4 相对介电常数Relative permittivity 4.84.8 4.04.0 4.24.2 5.15.1 线收缩率(%)Linear shrinkage (%) 5.3%5.3% 2.62%2.62% 4.5%4.5% 1.3%1.3%

以上实施例仅用以说明本发明的技术方案而非限制,尽管参照较佳实施例对本发明进行了详细说明,本领域的普通技术人员应当理解,可以在不脱离本发明的原理和精神的情况下可以对这些实施例进行多种变化、修改、替换和变型,本发明的范围由所附权利要求及其等同限定。The above embodiments are only used to illustrate the technical solutions of the present invention and not to limit them. Although the present invention has been described in detail with reference to the preferred embodiments, those of ordinary skill in the art should understand that the present invention can be implemented without departing from the principle and spirit of the present invention. Various changes, modifications, substitutions and alterations may be made to these embodiments, the scope of the invention being defined by the appended claims and their equivalents.

Claims (10)

1.一种利用多晶硅切割废料在低温下制备SiO2-Si3N4复合陶瓷的方法,其特征在于,包括以下步骤:1. a method of utilizing polysilicon cutting waste to prepare SiO 2 -Si 3 N 4 composite ceramics at low temperature, is characterized in that, comprises the following steps: (1)将多晶硅切割废料纯化处理,得到纯化后的多晶硅切割废料,其中Si纯度为2N级别;(1) purifying the polysilicon cutting waste to obtain purified polysilicon cutting waste, wherein the Si purity is 2N; (2)多晶硅切割废料的氮化处理:(2) Nitriding treatment of polysilicon cutting waste: 在步骤(1)得到纯化后的多晶硅切割废料中加入稀释剂,球磨混合后,进行气氛氮化,氮化反应后得到氮化产物;A diluent is added to the purified polysilicon cutting waste obtained in step (1), and after ball milling and mixing, atmosphere nitriding is carried out, and a nitriding product is obtained after nitriding reaction; (3)SiO2-Si3N4复合陶瓷的氨化烧制(3) Ammonia firing of SiO 2 -Si 3 N 4 composite ceramics 将步骤(2)中的氮化产物用研钵研磨,添加一定比例的SiO2、C、烧结助剂,球磨至物料混匀,烘干物料,冷等静压成型得到氨化前样品;在气氛管式炉设备中通入氨化气体后,程序升温至氨化反应的温度,恒温反应一段时间,氨化反应结束后,程序降温到室温,得到SiO2-Si3N4复合陶瓷。Grinding the nitrided product in step (2) with a mortar, adding a certain proportion of SiO 2 , C and sintering aid, ball milling until the material is mixed, drying the material, and cold isostatic pressing to obtain the sample before ammoniation; After the ammoniated gas is introduced into the atmosphere tube furnace equipment, the temperature is programmed to reach the temperature of the ammoniated reaction, and the reaction is kept constant for a period of time . 2.如权利要求1所述的方法,其特征在于,步骤(1)中,多晶硅切割废料的纯化处理过程为:多晶硅切割废料经烘干、粉碎、冲洗杂质、再次烘干、研磨、过筛得到粉体的过程。2. method as claimed in claim 1 is characterized in that, in step (1), the purification treatment process of polysilicon cutting waste is: polysilicon cutting waste is dried, pulverized, washed with impurities, dried again, ground, sieved The process of obtaining powder. 3.如权利要求1所述的方法,其特征在于,步骤(2)中,所述稀释剂为α-Si3N4或β-Si3N4,添加量不超过纯化后的多晶硅切割废料质量的20%。3. The method of claim 1, wherein in step (2), the diluent is α-Si 3 N 4 or β-Si 3 N 4 , and the addition amount does not exceed the purified polysilicon cutting waste 20% of the mass. 4.如权利要求1所述的方法,其特征在于,步骤(2)中,所述氮化反应中,氮化气体为氮气或氮氢混合气中的一种,其中,氮氢混合气中,氮气和氢气的体积比在75:25-95:5之间。4. The method of claim 1, wherein, in step (2), in the nitriding reaction, the nitriding gas is one of nitrogen gas or a nitrogen-hydrogen mixture, wherein, in the nitrogen-hydrogen mixture , the volume ratio of nitrogen and hydrogen is between 75:25-95:5. 5.如权利要求1所述的方法,其特征在于,步骤(2)中,所述氮化反应中,氮化设备采用程序控温的气氛管式炉,确保炉内温度以1-5℃/min的速度升温至1200-1450℃,然后恒温0.5-2.5h。5. The method according to claim 1, wherein, in step (2), in the nitriding reaction, the nitriding equipment adopts a temperature-controlled atmosphere tube furnace to ensure that the temperature in the furnace is 1-5 °C The temperature is raised to 1200-1450°C at the speed of /min, and then the temperature is kept constant for 0.5-2.5h. 6.如权利要求1所述的方法,其特征在于,步骤(3)中,氮化产物用研钵研磨至300目以下。6 . The method of claim 1 , wherein, in step (3), the nitrided product is ground to below 300 mesh with a mortar. 7 . 7.如权利要求1所述的方法,其特征在于,步骤(3)中,所述烧结助剂为MgO、Al2O3、Y2O3中的一种或几种。7 . The method of claim 1 , wherein, in step (3), the sintering aid is one or more of MgO, Al 2 O 3 and Y 2 O 3 . 8.如权利要求1所述的方法,其特征在于,步骤(3)中,所述的SiO2、C、烧结助剂添加量分别不超过氮化产物质量的100%、20%、20%。8 . The method of claim 1 , wherein in step (3), the addition amounts of the SiO 2 , C and sintering aids do not exceed 100%, 20%, and 20% of the quality of the nitrided product, respectively. 9 . . 9.如权利要求1所述的方法,其特征在于,步骤(3)中,所述的氨化气体为氨气、氮氨混合气、氢氨混合气及氮氢氨混合气中的一种,其中,使用混合气时,氨气的体积占比控制在50%以上。9. method as claimed in claim 1, is characterized in that, in step (3), described ammoniated gas is a kind of in ammonia, nitrogen-ammonia mixture, hydrogen-ammonia mixture and nitrogen-hydrogen-ammonia mixture , among which, when using mixed gas, the volume ratio of ammonia gas is controlled to be more than 50%. 10.如权利要求1所述的方法,其特征在于,步骤(3)中,氨化反应的温度为1100-1450℃,恒温保持1-3h;程序升温和程序降温的速率均为1-5℃/min。10. method as claimed in claim 1 is characterized in that, in step (3), the temperature of ammoniation reaction is 1100-1450 ℃, and constant temperature keeps 1-3h; °C/min.
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