CN111392704A - A kind of preparation method of optical grade aluminum metaphosphate - Google Patents
A kind of preparation method of optical grade aluminum metaphosphate Download PDFInfo
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Abstract
本发明技术方案提供了一种光学级偏磷酸铝的制备方法,包括如下步骤:将氢氧化铝或氧化铝与磷酸、水按一定比例发生反应,得到粗磷酸二氢铝溶液;调节粗磷酸二氢铝溶液的浓度,使其经过离子交换树脂,以脱除有色金属和杂质离子;将经过离子交换树脂后的溶液蒸发浓缩,提浓至40%以上;进行第一次洁净煅烧,以脱除游离水和结构水,得到偏磷酸铝中间体粉体;进行第二次洁净煅烧,获得光学级偏磷酸铝成品。本发明技术方案的制备方法对于原料氢氧化铝或氧化铝的适应性强,采用离子交换法除杂,间接加热洁净喷雾煅烧结合高温电炉洁净煅烧的方式,制备出的偏磷酸铝纯度较高,各项指标均满足光学玻璃和激光玻璃原料的要求。
The technical scheme of the present invention provides a preparation method of optical grade aluminum metaphosphate, comprising the following steps: reacting aluminum hydroxide or aluminum oxide with phosphoric acid and water in a certain proportion to obtain a crude aluminum dihydrogen phosphate solution; adjusting the crude dihydrogen phosphate solution; The concentration of aluminum hydride solution is passed through ion exchange resin to remove non-ferrous metals and impurity ions; the solution after passing through ion exchange resin is evaporated and concentrated to more than 40%; the first clean calcination is carried out to remove Free water and structured water are used to obtain the intermediate powder of aluminum metaphosphate; the second clean calcination is carried out to obtain the finished product of optical grade aluminum metaphosphate. The preparation method of the technical solution of the present invention has strong adaptability to the raw material aluminum hydroxide or alumina, adopts the ion exchange method to remove impurities, indirect heating and clean spray calcination combined with high temperature electric furnace clean calcination, and the prepared aluminum metaphosphate has high purity. All indicators meet the requirements of optical glass and laser glass raw materials.
Description
技术领域technical field
本发明涉及精细无机磷化工领域,具体涉及一种光学级偏磷酸铝的制备方法。The invention relates to the field of fine inorganic phosphorous chemical industry, in particular to a preparation method of optical grade aluminum metaphosphate.
背景技术Background technique
偏磷酸盐是二元磷酸盐中最稳定的磷酸盐,是制造磷酸盐玻璃的基础原料。高纯偏磷酸盐由于具有优良的透光性能,不仅可用于大功率激光器(如国家大科学工程~神光计划)中激光玻璃的重要原料,还是一些高级光学器材如相机镜头、高清摄像头、智能手机镜头和手机面板基板的重要原料。由于过渡金属Fe、Co、Ni等的存在会导致偏磷酸盐玻璃在近紫外到红外区域产生强吸收,影响玻璃的光学性能。因此,高纯偏磷酸盐原料的制备成为制造高性能激光玻璃的关键。Metaphosphate is the most stable phosphate among dibasic phosphates, and is the basic raw material for making phosphate glass. Due to its excellent light transmission properties, high-purity metaphosphates can not only be used as an important raw material for laser glass in high-power lasers (such as the National Science Project ~ Shenguang Project), but also some advanced optical equipment such as camera lenses, high-definition cameras, intelligent It is an important raw material for mobile phone lens and mobile phone panel substrate. Due to the presence of transition metals Fe, Co, Ni, etc., the metaphosphate glass will have strong absorption in the near-ultraviolet to infrared region, which will affect the optical properties of the glass. Therefore, the preparation of high-purity metaphosphate raw materials has become the key to the manufacture of high-performance laser glass.
虽然我国已是磷化工生产大国,但高附加的、精细的磷化工产品开发滞后,缺乏国际市场的竞争力。鉴于国际同行对我们实行技术封锁,我们只有自主创新,加强精细化磷化工产品的深度开发,提高产品的高科技含量,提高产品附加值,才能提高企业的经济效益。Although my country is already a big producer of phosphorus chemical products, the development of high-added and fine phosphorus chemical products is lagging behind and lacks competitiveness in the international market. In view of the technical blockade imposed on us by international counterparts, we can only improve the economic benefits of the enterprise by innovating independently, strengthening the in-depth development of fine phosphorus chemical products, improving the high-tech content of products, and increasing the added value of products.
专利CN201810111408.4公开了一种利用电子级磷酸、铝源(高纯氢氧化铝)经中间体一水酸式磷酸铝并吸湿风化得到酸式磷酸铝粉末进而煅烧得到高纯偏磷酸铝的方法,此法全流程须采用高纯原材料,并无化学提纯过程,方法具有显著的原料局限性,操作步骤繁琐,产品纯度也很难达到比较高的程度(如过渡金属杂质总量小于2ppm)。Patent CN201810111408.4 discloses a method of using electronic grade phosphoric acid and aluminum source (high-purity aluminum hydroxide) to obtain acid aluminum phosphate powder through intermediate acid aluminum phosphate monohydrate and hygroscopic weathering, and then calcining to obtain high-purity aluminum metaphosphate. The whole process of the method must use high-purity raw materials, and there is no chemical purification process. The method has significant raw material limitations, complicated operation steps, and it is difficult to achieve a relatively high level of product purity (for example, the total amount of transition metal impurities is less than 2ppm).
发明内容SUMMARY OF THE INVENTION
鉴于以上所述现有技术的现状,本发明需要解决的技术问题是提供一种制备光学级偏磷酸铝的方法,其制备出的偏磷酸铝的主要指标均能够满足制造光学玻璃和激光玻璃的要求。In view of the current situation of the above-mentioned prior art, the technical problem to be solved in the present invention is to provide a method for preparing optical grade aluminum metaphosphate, and the main indicators of the prepared aluminum metaphosphate can meet the requirements for manufacturing optical glass and laser glass. Require.
为解决上述技术问题,本发明技术方案提供了一种光学级偏磷酸铝的制备方法,包括如下步骤:In order to solve the above-mentioned technical problems, the technical solution of the present invention provides a preparation method of optical grade aluminum metaphosphate, comprising the following steps:
1)将氢氧化铝或氧化铝与磷酸、水按一定比例发生反应,得到粗磷酸二氢铝溶液;1) reacting aluminum hydroxide or aluminum oxide with phosphoric acid and water in a certain proportion to obtain a thick aluminum dihydrogen phosphate solution;
2)调节粗磷酸二氢铝溶液的浓度,使其经过离子交换树脂,以脱除有色金属和杂质离子;2) adjust the concentration of the crude aluminum dihydrogen phosphate solution to pass through the ion exchange resin to remove non-ferrous metals and impurity ions;
3)将经过离子交换树脂后的溶液蒸发浓缩,提浓至40%以上;3) Evaporating and concentrating the solution after passing through the ion exchange resin to more than 40%;
4)进行第一次洁净煅烧,以脱除游离水和结构水,得到偏磷酸铝中间体粉体;4) carry out clean calcination for the first time to remove free water and structured water to obtain aluminum metaphosphate intermediate powder;
5)进行第二次洁净煅烧,获得光学级偏磷酸铝成品。5) Carry out the second clean calcination to obtain the finished product of optical grade aluminum metaphosphate.
优选地,步骤1)中,氢氧化铝或氧化铝与所述磷酸的摩尔比为1:(5.9~6.1),磷酸与水的质量比为1:(0.6~1.5),反应温度为105℃~125℃。更为优选地,氢氧化铝或氧化铝与所述磷酸的摩尔比为1:(5.95~6.05),磷酸与水的质量比为1:(0.6~0.9),反应温度为110℃~120℃。Preferably, in step 1), the molar ratio of aluminum hydroxide or alumina to the phosphoric acid is 1:(5.9~6.1), the mass ratio of phosphoric acid to water is 1:(0.6~1.5), and the reaction temperature is 105° C. ~125°C. More preferably, the molar ratio of aluminum hydroxide or alumina to the phosphoric acid is 1:(5.95~6.05), the mass ratio of phosphoric acid and water is 1:(0.6~0.9), and the reaction temperature is 110℃~120℃ .
优选地,调节粗磷酸二氢铝溶液的浓度为9%~18%,经过离子交换树脂的流速为1L/min~5L/min。进一步优选地,调节粗磷酸二氢铝溶液的浓度为9%~14%,经过离子交换树脂的流速为2L/min~4L/min。Preferably, the concentration of the crude aluminum dihydrogen phosphate solution is adjusted to be 9% to 18%, and the flow rate through the ion exchange resin is 1L/min to 5L/min. Further preferably, the concentration of the crude aluminum dihydrogen phosphate solution is adjusted to be 9% to 14%, and the flow rate through the ion exchange resin is 2L/min to 4L/min.
优选地,所述离子交换树脂包括阳离子交换树脂和阴离子交换树脂,所述离子交换树脂包括阳离子交换树脂和阴离子交换树脂,所述阳离子交换树脂包括D401、D402、D403、D405、IONRESIN 35、IONRESIN 1600、IONRESIN 252中的一种或几种组合,所述阴离子交换树脂包括IONRESIN IRA400、IONRESIN IRA402、IONRESIN IRA900、IONRESIN IRA456、D407中的一种或几种组合。Preferably, the ion exchange resin includes cation exchange resin and anion exchange resin, the ion exchange resin includes cation exchange resin and anion exchange resin, and the cation exchange resin includes D401, D402, D403, D405, IONRESIN 35, IONRESIN 1600 , one or more combinations of IONRESIN 252, and the anion exchange resin includes one or more combinations of IONRESIN IRA400, IONRESIN IRA402, IONRESIN IRA900, IONRESIN IRA456, and D407.
优选地,步骤3)中,提浓至40%~50%。更优选地,提浓至42~47%。Preferably, in step 3), the concentration is 40% to 50%. More preferably, it is concentrated to 42-47%.
优选地,提浓后的磷酸二氢铝溶液以6L/min~15L/min的流速进入喷雾煅烧塔进行第一次洁净煅烧,其中进风温度为700℃~800℃,塔体上段温度为680℃~750℃,塔体中段温度为650℃~720℃,塔体下段温度为620℃~700℃,出风温度为400℃~500℃。Preferably, the concentrated aluminum dihydrogen phosphate solution enters the spray calcination tower at a flow rate of 6L/min~15L/min for the first clean calcination, wherein the inlet air temperature is 700°C~800°C, and the temperature of the upper section of the tower body is 680°C ℃~750℃, the temperature in the middle section of the tower body is 650℃~720℃, the temperature in the lower section of the tower body is 620℃~700℃, and the air outlet temperature is 400℃~500℃.
更进一步地,提浓后的磷酸二氢铝溶液以9L/min~12L/min的流速进入喷雾煅烧塔进行第一次洁净煅烧,其中进风温度为680℃~730℃,塔体上段温度为650℃~700℃,塔体中段温度为630℃~680℃,塔体下段温度为600℃~630℃,出风温度为380℃~430℃。为了保证产品品质,煅烧塔物料接触部分采用高纯氧化铝内衬,喷头采用钛钯合金制造(可杜绝喷雾煅烧过程中喷头对产品的污染),加热方式采用间接加热,高温尾气通过热交换器换热加热喷雾煅烧塔进风,整个系统热效率高,能耗低。Further, the concentrated aluminum dihydrogen phosphate solution enters the spray calcining tower at a flow rate of 9L/min~12L/min for the first clean calcination, wherein the inlet air temperature is 680 ℃~730 ℃, and the temperature of the upper section of the tower body is 650℃~700℃, the temperature in the middle section of the tower body is 630℃~680℃, the temperature in the lower section of the tower body is 600℃~630℃, and the air outlet temperature is 380℃~430℃. In order to ensure product quality, the material contact part of the calcining tower is lined with high-purity alumina, and the nozzle is made of titanium-palladium alloy (which can prevent the pollution of the nozzle to the product during the spray calcination process). The heating method adopts indirect heating, and the high-temperature exhaust gas passes through the heat exchanger The heat exchange heating spray calcination tower enters the air, the whole system has high thermal efficiency and low energy consumption.
在喷雾煅烧的过程中,为了确保物料不被污染,需要保证洁净煅烧,只能采用间接加热的方式,随之而来的问题是喷雾煅烧塔进风温度最高只能达到780℃~800℃(塔体温度只能达到700℃~740℃),在瞬时煅烧脱水的工况中,这个温度段对于偏磷酸铝的煅烧而言,是很难彻底脱水的,至多可以脱除98%的磷酸二氢铝结构水,需要更高的持久温度和进一步的煅烧设备脱除最终微量的结构水。因此,本发明采用二次煅烧法,在电炉中进行第二次洁净煅烧,电炉的煅烧温度为750℃~850℃,煅烧时间为4h~10h。In the process of spray calcination, in order to ensure that the material is not polluted, it is necessary to ensure clean calcination, and only indirect heating can be used. The temperature of the tower body can only reach 700℃~740℃), in the condition of instantaneous calcination and dehydration, it is difficult to completely dehydrate the calcination of aluminum metaphosphate in this temperature range, and at most 98% of diphosphate can be removed. Hydro-aluminum structural water requires higher persistent temperature and further calcination equipment to remove the final trace amount of structural water. Therefore, the present invention adopts the secondary calcination method, and conducts the secondary clean calcination in an electric furnace, the calcination temperature of the electric furnace is 750°C to 850°C, and the calcination time is 4h to 10h.
进一步地,步骤e中电炉煅烧温度为780℃~840℃,煅烧时间6h~9h。炉膛采用高纯氧化铝或高纯石英材料作为内衬。Further, in step e, the calcination temperature of the electric furnace is 780°C to 840°C, and the calcination time is 6h to 9h. The furnace is lined with high-purity alumina or high-purity quartz material.
本发明技术方案的光学级偏磷酸铝的制备方法具有如下有益效果:对于原料氢氧化铝或氧化铝、磷酸的适应性强,采用离子交换法除杂,间接加热洁净喷雾煅烧结合高温电炉洁净煅烧的方式,过渡金属杂质总量可控制到2ppm以下,可制造出超纯度的偏磷酸铝,各项指标均满足光学玻璃和激光玻璃原料的要求。The preparation method of optical grade aluminum metaphosphate of the technical scheme of the present invention has the following beneficial effects: strong adaptability to raw material aluminum hydroxide, aluminum oxide and phosphoric acid, ion exchange method is used to remove impurities, indirect heating and clean spray calcination combined with high temperature electric furnace clean calcination In this way, the total amount of transition metal impurities can be controlled below 2ppm, and ultra-purity aluminum metaphosphate can be produced. All indicators meet the requirements of optical glass and laser glass raw materials.
附图说明Description of drawings
为了更清楚地说明本发明实施例或现有技术中的技术方案,下面将对实施例描述中所需要使用的附图作简单地介绍,显而易见地,下面描述中的附图仅仅是本发明的一些实施例,对于本领域普通技术人员来讲,在不付出创造性劳动性的前提下,还可以根据这些附图获得其他的附图。In order to illustrate the embodiments of the present invention or the technical solutions in the prior art more clearly, the following briefly introduces the accompanying drawings used in the description of the embodiments. Obviously, the drawings in the following description are only for the present invention. In some embodiments, for those of ordinary skill in the art, other drawings can also be obtained according to these drawings without any creative effort.
图1为本发明技术方案的光学级偏磷酸铝的制备方法流程图。Fig. 1 is the flow chart of the preparation method of the optical grade aluminum metaphosphate of the technical scheme of the present invention.
具体实施方式Detailed ways
以下将结合附图对本发明的构思、具体结构及产生的技术效果作进一步说明,以充分地了解本发明的目的、特征和效果。The concept, specific structure and technical effects of the present invention will be further described below in conjunction with the accompanying drawings, so as to fully understand the purpose, characteristics and effects of the present invention.
如图1所示,本发明技术方案的光学级偏磷酸铝的制备方法,包括如下步骤:As shown in Figure 1, the preparation method of the optical grade aluminum metaphosphate of the technical scheme of the present invention comprises the following steps:
1)将氢氧化铝或氧化铝与磷酸、水按一定比例发生反应(即图1中的加热逐步反应),得到粗磷酸二氢铝溶液;1) reacting aluminum hydroxide or aluminum oxide with phosphoric acid and water in a certain proportion (that is, the heating stepwise reaction in Fig. 1) to obtain a thick aluminum dihydrogen phosphate solution;
2)调节粗磷酸二氢铝溶液的浓度,使其经过离子交换树脂,以脱除有色金属和杂质离子;2) adjust the concentration of the crude aluminum dihydrogen phosphate solution to pass through the ion exchange resin to remove non-ferrous metals and impurity ions;
3)将经过离子交换树脂后的溶液蒸发浓缩,提浓至40%以上;3) Evaporating and concentrating the solution after passing through the ion exchange resin to more than 40%;
4)进行第一次洁净煅烧,以脱除游离水和结构水,得到偏磷酸铝中间体粉体;4) carry out clean calcination for the first time to remove free water and structured water to obtain aluminum metaphosphate intermediate powder;
5)进行第二次洁净煅烧,获得光学级偏磷酸铝成品。5) Carry out the second clean calcination to obtain the finished product of optical grade aluminum metaphosphate.
实施例1Example 1
本发明实施例的光学级偏磷酸铝的制备方法,包括以下步骤:The preparation method of the optical grade aluminum metaphosphate of the embodiment of the present invention comprises the following steps:
1)100kg含量为97.5%的氧化铝逐步加入至由664.1kg 85%的工业磷酸和464.9kg水勾兑而成的稀磷酸中,控制反应温度为110℃~115℃,得到粗磷酸二氢铝溶液;1) 100kg content is that the alumina of 97.5% is gradually added in the dilute phosphoric acid that is blended by 664.1kg 85% industrial phosphoric acid and 464.9kg water, and the control reaction temperature is 110 ℃~115 ℃, obtains thick aluminum dihydrogen phosphate solution ;
2)调节粗磷酸二氢铝溶液的浓度到12%,以4L/min的流速经过一组填充了D403、D405、IONRESIN 35型阳离子交换树脂和特别甄选的IONRESIN IRA402、IONRESIN IRA900型阴离子交换树脂的复合离子交换装置,以脱除Fe、Mn、Pb、Cr、Cu、Ni、Co等有色金属和Cl-、硫酸根等杂质;2) Adjust the concentration of the crude aluminum dihydrogen phosphate solution to 12%, and pass through a group of cation exchange resins filled with D403, D405, IONRESIN 35 type cation exchange resins and specially selected IONRESIN IRA402, IONRESIN IRA900 type anion exchange resins at a flow rate of 4L/min. Composite ion exchange device to remove non-ferrous metals such as Fe, Mn, Pb, Cr, Cu, Ni, Co, and impurities such as Cl- and sulfate;
3)将经过离子交换树脂后的溶液蒸发浓缩,提浓至45%;3) Evaporating and concentrating the solution after the ion exchange resin to 45%;
4)提浓后的磷酸二氢铝溶液通过工业蠕动泵控制,以10L/min流速进入喷雾煅烧塔内,控制煅烧塔进风温度为700℃~720℃,塔体上段温度为660℃~690℃,塔体中段温度为630℃~660℃,塔体下段温度为600℃~620℃,出风温度为390℃~420℃,得到515kg偏磷酸铝中间体粉体;4) The concentrated aluminum dihydrogen phosphate solution is controlled by an industrial peristaltic pump, and enters the spray calcination tower at a flow rate of 10L/min. ℃, the temperature in the middle section of the tower body is 630 ℃~660 ℃, the temperature in the lower section of the tower body is 600 ℃~620 ℃, the air outlet temperature is 390 ℃~420 ℃, obtain 515kg of aluminum metaphosphate intermediate powder;
5)偏磷酸铝中间体粉体在内衬高纯刚玉材料的电炉内,在800℃下煅烧6h,得到光学级偏磷酸铝成品492kg,综合收率为97.5%。5) The aluminum metaphosphate intermediate powder was calcined in an electric furnace lined with high-purity corundum material at 800° C. for 6 hours to obtain 492 kg of optical grade aluminum metaphosphate products, with a comprehensive yield of 97.5%.
实施例2Example 2
本发明实施例的光学级偏磷酸铝的制备方法,包括以下步骤:The preparation method of the optical grade aluminum metaphosphate of the embodiment of the present invention comprises the following steps:
1)120kg含量为96%的氧化铝逐步加入至由780kg 85%的工业磷酸和546kg水勾兑而成的稀磷酸中,控制反应温度为110℃~115℃,得到粗磷酸二氢铝溶液;1) 120kg content is that 96% alumina is gradually added into the dilute phosphoric acid that is blended by 780kg 85% industrial phosphoric acid and 546kg water, and the control reaction temperature is 110 ℃~115 ℃, obtains thick aluminum dihydrogen phosphate solution;
2)调节粗磷酸二氢铝溶液的浓度到10%,以5L/min的流速经过一组填充了铝盐改性的D401、D402型阳离子交换树脂和特别甄选的IONRESIN IRA456、D407型阴离子交换树脂的复合离子交换装置,以脱除Fe、Mn、Pb、Cr、Cu、Ni、Co等有色金属和Cl-、硫酸根等杂质;2) Adjust the concentration of the crude aluminum dihydrogen phosphate solution to 10%, and pass through a group of D401 and D402 cation exchange resins modified with aluminum salts and specially selected IONRESIN IRA456 and D407 anion exchange resins at a flow rate of 5L/min. The composite ion exchange device is used to remove non-ferrous metals such as Fe, Mn, Pb, Cr, Cu, Ni, Co and impurities such as Cl- and sulfate;
3)将经过离子交换树脂后的溶液蒸发浓缩,提浓至42%;3) Evaporating and concentrating the solution after the ion exchange resin to 42%;
4)提浓后的磷酸二氢铝溶液通过工业蠕动泵控制,以12L/min流速进入喷雾煅烧塔内,控制煅烧塔进风温度为720℃~740℃,塔体上段温度为670℃~690℃,塔体中段温度为640℃~665℃,塔体下段温度为610℃~625℃,出风温度为400℃~420℃,得到602kg偏磷酸铝中间体粉体;4) The concentrated aluminum dihydrogen phosphate solution is controlled by an industrial peristaltic pump, and enters the spray calcination tower with a flow rate of 12L/min. ℃, the temperature in the middle section of the tower body is 640 ℃~665 ℃, the temperature in the lower section of the tower body is 610 ℃~625 ℃, the air outlet temperature is 400 ℃~420 ℃, obtain 602kg of aluminum metaphosphate intermediate powder;
5)偏磷酸铝中间体粉体在内衬高纯刚玉材料的电炉内,在820℃下煅烧5h,得到光学级偏磷酸铝成品572kg,综合收率为95.9%。5) The aluminum metaphosphate intermediate powder was calcined at 820° C. for 5 hours in an electric furnace lined with high-purity corundum material to obtain 572 kg of optical grade aluminum metaphosphate products, with a comprehensive yield of 95.9%.
实施例3Example 3
本发明实施例的光学级偏磷酸铝的制备方法,包括以下步骤:The preparation method of the optical grade aluminum metaphosphate of the embodiment of the present invention comprises the following steps:
1)140kg含量为97%的氧化铝逐步加入至由928.2kg 85%的工业磷酸和649.8kg水勾兑而成的稀磷酸中,控制反应温度为112℃~116℃,得到粗磷酸二氢铝溶液;1) 140kg content is that the alumina of 97% is gradually added in the dilute phosphoric acid that is blended by 928.2kg 85% industrial phosphoric acid and 649.8kg water, and the control reaction temperature is 112 ℃~116 ℃, obtains thick aluminum dihydrogen phosphate solution ;
2)调节粗磷酸二氢铝溶液的浓度到11%,以4.5L/min的流速经过一组填充了铝盐改性的D402、D403、D405型阳离子交换树脂和特别甄选的IONRESIN IRA400、IONRESINIRA402型阴离子交换树脂的复合离子交换装置,以脱除Fe、Mn、Pb、Cr、Cu、Ni、Co等有色金属和Cl-、硫酸根等杂质;2) Adjust the concentration of the crude aluminum dihydrogen phosphate solution to 11%, and pass through a group of D402, D403, D405 cation exchange resins modified with aluminum salts and specially selected IONRESIN IRA400 and IONRESINIRA402 types at a flow rate of 4.5L/min. Composite ion exchange device of anion exchange resin to remove non-ferrous metals such as Fe, Mn, Pb, Cr, Cu, Ni, Co and impurities such as Cl- and sulfate;
3)将经过离子交换树脂后的溶液蒸发浓缩,提浓至46%;3) Evaporating and concentrating the solution after the ion exchange resin to 46%;
4)提浓后的磷酸二氢铝溶液通过工业蠕动泵控制,以11L/min流速进入喷雾煅烧塔内,控制煅烧塔进风温度为720℃~750℃,塔体上段温度为680℃~700℃,塔体中段温度为650℃~670℃,塔体下段温度为620℃~640℃,出风温度为405℃~420℃,得到710kg偏磷酸铝中间体粉体;4) The concentrated aluminum dihydrogen phosphate solution is controlled by an industrial peristaltic pump, and enters the spray calcination tower at a flow rate of 11 L/min. ℃, the temperature in the middle section of the tower body is 650 ℃~670 ℃, the temperature in the lower section of the tower body is 620 ℃~640 ℃, the air outlet temperature is 405 ℃~420 ℃, obtains 710kg of aluminum metaphosphate intermediate powder;
5)偏磷酸铝中间体粉体在内衬高纯刚玉材料的电炉内,在790℃下煅烧7h,得到光学级偏磷酸铝成品668kg,综合收率为95.1%。5) The aluminum metaphosphate intermediate powder was calcined at 790° C. for 7 hours in an electric furnace lined with high-purity corundum material to obtain 668 kg of optical grade aluminum metaphosphate products, with a comprehensive yield of 95.1%.
实施例4Example 4
本发明实施例的光学级偏磷酸铝的制备方法,包括以下步骤:The preparation method of the optical grade aluminum metaphosphate of the embodiment of the present invention comprises the following steps:
1)200kg含量为96%的氧化铝逐步加入至由1308.8kg 85%的工业磷酸和916.2kg水勾兑而成的稀磷酸中,控制反应温度为110℃~115℃,得到粗磷酸二氢铝溶液;1) 200kg of alumina with a content of 96% is gradually added to the dilute phosphoric acid that is blended by 1308.8kg 85% of industrial phosphoric acid and 916.2kg of water, and the controlled reaction temperature is 110°C to 115°C to obtain a crude aluminum dihydrogen phosphate solution ;
2)调节粗磷酸二氢铝溶液的浓度到12%,以4L/min的流速经过一组填充了铝盐改性的D405、IONRESIN 1600、IONRESIN 252型阳离子交换树脂和特别甄选的IONRESINIRA400、IONRESIN IRA402、IONRESIN IRA900型阴离子交换树脂的复合离子交换装置,以脱除Fe、Mn、Pb、Cr、Cu、Ni、Co等有色金属和Cl-、硫酸根等杂质;2) Adjust the concentration of the crude aluminum dihydrogen phosphate solution to 12%, and pass through a group of D405, IONRESIN 1600, IONRESIN 252 cation exchange resins and specially selected IONRESINIRA400, IONRESIN IRA402 filled with aluminum salts at a flow rate of 4L/min , IONRESIN IRA900 type anion exchange resin composite ion exchange device to remove Fe, Mn, Pb, Cr, Cu, Ni, Co and other non-ferrous metals and Cl- , sulfate and other impurities;
3)将经过离子交换树脂后的溶液蒸发浓缩,提浓至45%;3) Evaporating and concentrating the solution after the ion exchange resin to 45%;
4)提浓后的磷酸二氢铝溶液通过工业蠕动泵控制,以12L/min流速进入喷雾煅烧塔内,控制煅烧塔进风温度为730℃~760℃,塔体上段温度为690℃~720℃,塔体中段温度为650℃~670℃,塔体下段温度为615℃~630℃,出风温度为400℃~420℃,得到989kg偏磷酸铝中间体粉体;4) The concentrated aluminum dihydrogen phosphate solution is controlled by an industrial peristaltic pump, and enters the spray calcination tower with a flow rate of 12L/min. ℃, the temperature in the middle section of the tower body is 650 ℃~670 ℃, the temperature in the lower section of the tower body is 615 ℃~630 ℃, the air outlet temperature is 400 ℃~420 ℃, obtain 989kg of aluminum metaphosphate intermediate powder;
5)偏磷酸铝中间体粉体在内衬高纯刚玉材料的电炉内,在840℃下煅烧5h,得到光学级偏磷酸铝成品949kg,综合收率为95.5%。5) The aluminum metaphosphate intermediate powder was calcined at 840° C. for 5 hours in an electric furnace lined with high-purity corundum material to obtain 949 kg of optical grade aluminum metaphosphate products, with a comprehensive yield of 95.5%.
实施例5Example 5
本发明实施例的光学级偏磷酸铝的制备方法,包括以下步骤:The preparation method of the optical grade aluminum metaphosphate of the embodiment of the present invention comprises the following steps:
1)170kg含量为98%的氧化铝逐步加入至由1127.6kg 85%的工业磷酸和789.4kg水勾兑而成的稀磷酸中,1917kg含量为50%的工业磷酸中,控制反应温度为113℃~118℃,得到粗磷酸二氢铝溶液;1) 170kg of alumina with a content of 98% is gradually added to the dilute phosphoric acid blended by 1127.6kg of 85% industrial phosphoric acid and 789.4kg of water, and in 1917kg of industrial phosphoric acid with a content of 50%, the control reaction temperature is 113 ℃~ 118 ° C to obtain crude aluminum dihydrogen phosphate solution;
2)调节粗磷酸二氢铝溶液的浓度到12.5%,以4.2L/min的流速经过一组填充了铝盐改性的IONRESIN 35、IONRESIN 1600型阳离子交换树脂和特别甄选的IONRESIN IRA900、IONRESIN IRA456型阴离子交换树脂的复合离子交换装置,以脱除Fe、Mn、Pb、Cr、Cu、Ni、Co等有色金属和Cl-、硫酸根等杂质;2) Adjust the concentration of the crude aluminum dihydrogen phosphate solution to 12.5%, pass through a group of IONRESIN 35, IONRESIN 1600 cation exchange resins modified with aluminum salts and specially selected IONRESIN IRA900, IONRESIN IRA456 at a flow rate of 4.2L/min Type anion exchange resin composite ion exchange device to remove Fe, Mn, Pb, Cr, Cu, Ni, Co and other non-ferrous metals and Cl- , sulfate and other impurities;
3)将经过离子交换树脂后的溶液蒸发浓缩,提浓至44%;3) Evaporating and concentrating the solution after the ion exchange resin to 44%;
4)提浓后的磷酸二氢铝溶液通过工业蠕动泵控制,以11L/min流速进入喷雾煅烧塔内,控制煅烧塔进风温度为740℃~770℃,塔体上段温度为700℃~730℃,塔体中段温度为660℃~680℃,塔体下段温度为630℃~650℃,出风温度为410℃~430℃,得到854kg偏磷酸铝中间体粉体;4) The concentrated aluminum dihydrogen phosphate solution is controlled by an industrial peristaltic pump, and enters the spray calcination tower with a flow rate of 11 L/min. ℃, the temperature in the middle section of the tower body is 660 ℃~680 ℃, the temperature in the lower section of the tower body is 630 ℃~650 ℃, the air outlet temperature is 410 ℃~430 ℃, obtain 854kg of aluminum metaphosphate intermediate powder;
5)偏磷酸铝中间体粉体在内衬高纯刚玉材料的电炉内,在850℃下煅烧4.5h,得到光学级偏磷酸铝成品827kg,综合收率为95.9%。5) The aluminum metaphosphate intermediate powder was calcined in an electric furnace lined with high-purity corundum material at 850° C. for 4.5 hours to obtain 827 kg of optical grade aluminum metaphosphate products, with a comprehensive yield of 95.9%.
将实施例1~5制得的偏磷酸铝样品进行分析,结果如表1所示:The aluminum metaphosphate samples prepared in Examples 1 to 5 were analyzed, and the results were shown in Table 1:
表1偏磷酸铝样品分析Table 1 Analysis of aluminum metaphosphate samples
从表1中可看出,实施例1~5制备的偏磷酸铝中,Fe2O3、Cu、Co、Cr、Mn、Ni、Pb等10个关键杂质指标含量总和不超过5ppm,其中Co、Cr、Mn、Ni、Pb等含量总和不超过1ppm,Cu含量不超过0.2ppm,Fe2O3含量不超过2ppm,Cl-、硫酸根含量总和不超过100ppm,Al2O3含量19±0.5%、P2O5含量81±0.5%。As can be seen from Table 1, in the aluminum metaphosphates prepared in Examples 1-5, the total content of 10 key impurity indexes such as Fe 2 O 3 , Cu, Co, Cr, Mn, Ni, Pb, etc. does not exceed 5ppm, of which Co The total content of , Cr, Mn, Ni, Pb, etc. should not exceed 1ppm, the Cu content should not exceed 0.2ppm, the Fe 2 O 3 content should not exceed 2 ppm, the total content of Cl - and sulfate should not exceed 100 ppm, and the Al 2 O 3 content should not exceed 19±0.5 %, P 2 O 5 content 81±0.5%.
综上可知,本发明制备的偏磷酸铝主含量高、杂质含量很低、质量稳定、颗粒度均匀,各项指标均符合激光玻璃和光学玻璃原料的指标要求,且本发明的光学级偏磷酸铝的制备方法高效且简便、生产成本低。To sum up, the aluminum metaphosphate prepared by the present invention has high main content, very low impurity content, stable quality and uniform particle size, and each index meets the index requirements of laser glass and optical glass raw materials, and the optical grade metaphosphoric acid of the present invention is The preparation method of aluminum is efficient and simple, and the production cost is low.
以上详细描述了本发明的具体实施例,应当理解,本领域的普通技术人员无需创造性劳动就可以根据本发明的构思作出诸多修改和变化。因此,凡本技术领域中技术人员依本发明的构思在现有技术的基础上通过逻辑分析、推理或者有限的实验可以得到的技术方案,皆应在由权利要求书所确定的保护范围内。The specific embodiments of the present invention are described above in detail, and it should be understood that those skilled in the art can make many modifications and changes according to the concept of the present invention without creative efforts. Therefore, all technical solutions that can be obtained by those skilled in the art through logical analysis, reasoning or limited experiments on the basis of the prior art according to the concept of the present invention shall fall within the protection scope determined by the claims.
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