CN104888866B - A kind of silicon magnesium complexes carrier and preparation method thereof - Google Patents
A kind of silicon magnesium complexes carrier and preparation method thereof Download PDFInfo
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Abstract
本发明涉及一种催化剂载体,特别涉及一种硅镁复合物载体及其制备方法。该硅镁复合物载体由硅、铝的氧化物和镁的碳酸盐及其氧化物的复合物,或硅的氧化物和镁的碳酸盐及其氧化物的复合物为载体,其中Si:Al:Mg=5‑7:0‑3:2‑5;本发明制备方法简单,并且活性高,强度高,选择性好;并且本发明采用共沉淀法制得载体,增大了载体的比表面积和细孔容积。The invention relates to a catalyst carrier, in particular to a silicon-magnesium composite carrier and a preparation method thereof. The silicon-magnesium composite carrier is supported by a composite of silicon, aluminum oxide, magnesium carbonate and its oxide, or a composite of silicon oxide, magnesium carbonate and its oxide, wherein Si : Al: Mg=5-7:0-3:2-5; the preparation method of the present invention is simple, and has high activity, high strength, and good selectivity; surface area and pore volume.
Description
(一)技术领域(1) Technical field
本发明涉及一种催化剂载体,特别涉及一种硅镁复合物载体及其制备方法。The invention relates to a catalyst carrier, in particular to a silicon-magnesium composite carrier and a preparation method thereof.
(二)背景技术(2) Background technology
催化剂载体又称担体(support),是负载型催化剂的组成之一。催化活性组分担载在载体表面上,载体主要用于支持活性组分,使催化剂具有特定的物理性状,而载体本身一般并不具有催化活性。多数载体是催化剂工业中的产品,常用的有氧化铝载体、硅胶载体、活性炭载体及某些天然产物如浮石、硅藻土等。目前,多采用压球法或挤条法制得载体母球,然后经活化焙烧和/或过热蒸汽扩孔处理获得最终的催化剂载体,这种工艺的缺点难以达到理想的细孔直径,比表面积和孔容积较小,从而造成载体的活性下降和交换容积降低,在催化合成产品时,就会影响单位体积的产量,并使载体的用量增加。The catalyst carrier, also known as the support, is one of the components of the supported catalyst. Catalytically active components are carried on the surface of the carrier, and the carrier is mainly used to support the active component to make the catalyst have specific physical properties, while the carrier itself generally does not have catalytic activity. Most carriers are products in the catalyst industry, commonly used are alumina carriers, silica gel carriers, activated carbon carriers, and some natural products such as pumice, diatomaceous earth, etc. At present, most of the carrier cue balls are prepared by pelletizing method or extruding method, and then the final catalyst carrier is obtained by activation roasting and/or superheated steam pore expansion treatment. The disadvantages of this process are that it is difficult to achieve the ideal pore diameter, specific surface area and The small pore volume will result in a decrease in the activity of the carrier and a decrease in the exchange volume, which will affect the output per unit volume and increase the amount of the carrier when catalyzing the synthesis of products.
(三)发明内容(3) Contents of the invention
本发明为了弥补现有技术的不足,提供了一种硅镁复合物载体及其制备方法。In order to make up for the deficiencies of the prior art, the invention provides a silicon-magnesium composite carrier and a preparation method thereof.
本发明是通过如下技术方案实现的:The present invention is achieved through the following technical solutions:
一种硅镁复合物载体,其特征在于:包括由硅、铝的氧化物和镁的碳酸盐及镁的氧化物组成的复合物,或由硅的氧化物和镁的碳酸盐及镁的氧化物组成的复合物为载体。A silicon-magnesium composite carrier, characterized in that: it includes a composite composed of silicon, aluminum oxide, magnesium carbonate, and magnesium oxide, or a silicon oxide, magnesium carbonate, and magnesium The composite composed of oxides is used as the carrier.
上述硅镁复合物载体的制备方法,包括以下步骤:The preparation method of above-mentioned silicon-magnesium composite carrier comprises the following steps:
(1)在烧杯中依次加入硅酸钠水溶液1000ml和20%氨水,通过20%氨水控制体系PH值为9-11,搅拌下升温至50-60℃;(1) Add 1000ml of sodium silicate aqueous solution and 20% ammonia water to the beaker in sequence, control the pH value of the system to 9-11 through 20% ammonia water, and raise the temperature to 50-60°C under stirring;
(2)在上述混合液中加入硝酸镁或硝酸镁和硝酸铝的混合溶液500ml混合均匀,搅拌1h后加入20%盐酸将体系pH值调整至4-6,再搅拌1h;(2) Add 500ml of magnesium nitrate or a mixed solution of magnesium nitrate and aluminum nitrate to the above mixture and mix evenly. After stirring for 1 hour, add 20% hydrochloric acid to adjust the pH value of the system to 4-6, and then stir for 1 hour;
(3)搅拌结束后,再向体系中加入2mol/L的碳酸铵溶液将体系pH值调整至8后,升温至80-90℃,搅拌6小时,然后老化40h得到沉淀物;(3) After the stirring is completed, add 2mol/L ammonium carbonate solution to the system to adjust the pH value of the system to 8, then raise the temperature to 80-90°C, stir for 6 hours, and then age for 40 hours to obtain the precipitate;
(4)将沉淀物过滤洗涤后于100-130℃下烘干,于400-600℃焙烧5小时,粉碎过200目筛,制得载体。(4) Filter and wash the precipitate, dry it at 100-130°C, bake it at 400-600°C for 5 hours, and crush it through a 200-mesh sieve to obtain the carrier.
上述硅酸钠水溶液浓度为:以二氧化硅计浓度为40-58克二氧化硅/升硅酸钠水溶液。The concentration of the above-mentioned sodium silicate aqueous solution is: calculated as silicon dioxide, the concentration is 40-58 grams of silicon dioxide per liter of sodium silicate aqueous solution.
上述步骤(2)中加入的硝酸镁的浓度为:以氧化镁计浓度为70-85克氧化镁/升硝酸镁。The concentration of the magnesium nitrate added in the above-mentioned step (2) is: in magnesium oxide, the concentration is 70-85 grams of magnesium oxide/liter of magnesium nitrate.
上述步骤(2)中加入的硝酸铝的浓度为:以氧化铝计浓度为50-100克氧化铝/升。The concentration of the aluminum nitrate added in the above step (2) is: calculated as alumina, the concentration is 50-100 grams of alumina/liter.
其中,所述载体孔容为0.6-1.5 ml/g,比表面积为55-130 m2/g。Wherein, the carrier has a pore volume of 0.6-1.5 ml/g and a specific surface area of 55-130 m 2 /g.
所述载体中硅、铝、镁的质量比例为,硅:铝:镁=5-7:0-3:2-5。The mass ratio of silicon, aluminum and magnesium in the carrier is silicon:aluminum:magnesium=5-7:0-3:2-5.
本发明的有益效果是:本发明提供了一种硅镁复合物载体,其中Si:Al:Mg=5-7:0-3:2-5;本发明制备方法简单,并且活性高,强度高,选择性好;并且本发明采用共沉淀法制得载体,增大了载体的比表面积和细孔容积。The beneficial effects of the present invention are: the present invention provides a silicon-magnesium composite carrier, wherein Si:Al:Mg=5-7:0-3:2-5; the preparation method of the present invention is simple, and has high activity and high strength , good selectivity; and the present invention adopts the co-precipitation method to prepare the carrier, which increases the specific surface area and pore volume of the carrier.
(四)具体实施方式(4) Specific implementation methods
实施例1:Example 1:
在一沉淀容器内依次加入以二氧化硅计浓度为44克二氧化硅/升的硅酸钠水溶液(水玻璃,以下同,青岛泡花碱厂产品)1000ml,以20%氨水(开元市化学试剂厂产品)控制体系pH值为10-11,搅拌下升温至60℃后,加入以氧化镁计浓度为71.3克氧化镁/升的硝酸镁(天津市耀华试剂厂产品)溶液250ml和以氧化铝计浓度为99.7克氧化铝/升的硝酸铝(沈阳市试剂一厂产品)溶液250ml混合液,在45-60℃下搅拌1小时后,使用20%盐酸再调整pH值为4-6,搅拌1小时,以2M的碳酸铵溶液调整pH值为8后,升温至80-90℃,再继续搅拌6小时,然后卸料,老化40小时,过滤洗涤,于125℃烘干。于550℃焙烧5小时后,经粉碎过200目筛,制得载体SA。Add 1000ml of sodium silicate aqueous solution (water glass, the same below, product of Qingdao Soda Soda Factory) with a concentration of 44 grams of silicon dioxide/liter in terms of silicon dioxide successively in a precipitation container, and add 1000ml of sodium silicate solution with 20% ammonia water (Kaiyuan Chemical Industry Co., Ltd.) Reagent factory product) to control the pH value of the system to 10-11, after stirring the temperature to 60°C, add 250ml of magnesium nitrate solution (product of Tianjin Yaohua Reagent Factory) and the following 250ml mixed solution of aluminum nitrate (product of Shenyang Reagent No. 1 Factory) solution with an alumina meter concentration of 99.7g/l, stirred at 45-60°C for 1 hour, then adjusted the pH value to 4-6 with 20% hydrochloric acid , stirred for 1 hour, adjusted the pH value to 8 with 2M ammonium carbonate solution, raised the temperature to 80-90°C, continued to stir for 6 hours, then unloaded, aged for 40 hours, filtered and washed, and dried at 125°C. After calcining at 550°C for 5 hours, the carrier S A was obtained by crushing and passing through a 200-mesh sieve.
实施例2:Example 2:
在一沉淀容器内依次加入以二氧化硅计浓度为50.6克二氧化硅/升的硅酸钠(青岛泡花碱厂产品)水溶液1000ml,以20%氨水(开元市化学试剂厂产品)控制体系pH值为10-11,搅拌下升温至60℃后,加入以氧化镁计浓度为80.7克氧化镁/升的硝酸镁(天津市耀华试剂厂产品)溶液250ml和以氧化铝计浓度为55.9克氧化铝/升硝酸铝(沈阳市试剂一厂产品)溶液250ml混合液,在45-60℃下搅拌1小时后,使用20%盐酸再调整pH值为4-6,搅拌1小时,以2M的碳酸铵溶液调整pH值为8后,升温至80-90℃,再继续搅拌6小时,然后卸料,老化40小时,过滤洗涤,于125℃烘干。于550℃焙烧5小时后,经粉碎过200目筛,制得载体SB。Add 1000ml of sodium silicate (product of Qingdao Soda Soda Factory) aqueous solution with a concentration of 50.6 grams of silicon dioxide per liter in a sedimentation container, and control the system with 20% ammonia water (product of Kaiyuan Chemical Reagent Factory). The pH value is 10-11. After heating up to 60°C under stirring, add 250ml of magnesium nitrate solution (product of Tianjin Yaohua Reagent Factory) with a concentration of 80.7 grams of magnesium oxide per liter as magnesium oxide and a solution of 55.9 grams of magnesium oxide as aluminum oxide. gram of alumina/liter of aluminum nitrate (product of Shenyang Reagent No. After adjusting the pH value of the ammonium carbonate solution to 8, the temperature was raised to 80-90°C, and the stirring was continued for 6 hours, then unloaded, aged for 40 hours, filtered and washed, and dried at 125°C. After calcining at 550°C for 5 hours, the carrier S B was obtained by crushing and passing through a 200-mesh sieve.
实施例3:Example 3:
在一沉淀容器内依次加入以氧化硅计浓度为55.2克氧化硅/升的硅酸钠(青岛泡花碱厂产品)水溶液1000ml,以20%氨水(开元市化学试剂厂产品)控制体系pH值为10-11,搅拌下升温至60℃后,加入以氧化镁计浓度为81.0克氧化镁/升的硝酸镁(天津市耀华试剂厂产品)溶液500ml,在45-60℃下搅拌1小时后,使用20%盐酸再调整pH值为4-6,搅拌1小时,以2M的碳酸铵溶液调整pH值为8后,升温至80-90℃,再继续搅拌6小时,然后卸料,老化40小时,过滤洗涤,于125℃烘干。于550℃焙烧5小时后,经粉碎过200目筛,制得载体SC。Add 1000ml of sodium silicate (product of Qingdao Soda Soda Factory) aqueous solution with a concentration of 55.2 grams of silicon oxide per liter in a sedimentation container in sequence, and control the pH value of the system with 20% ammonia water (product of Kaiyuan Chemical Reagent Factory) After heating to 60°C under stirring, add 500ml of magnesium nitrate solution (produced by Tianjin Yaohua Reagent Factory) with a concentration of 81.0 grams of magnesium oxide/liter in terms of magnesium oxide, and stir for 1 hour at 45-60°C Finally, use 20% hydrochloric acid to adjust the pH value to 4-6, stir for 1 hour, adjust the pH value to 8 with 2M ammonium carbonate solution, raise the temperature to 80-90°C, and continue stirring for 6 hours, then unload and age After 40 hours, filter and wash, and dry at 125°C. After calcining at 550° C for 5 hours, the carrier SC was obtained by crushing and passing through a 200-mesh sieve.
表1 本发明各实施例中载体的组分含量Table 1 The component content of the carrier in each embodiment of the present invention
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---|---|---|---|---|
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CN1907567A (en) * | 2006-08-16 | 2007-02-07 | 天津化工研究设计院 | Forming method for porous composite metallic oxide catalytic carrier |
CN101613110A (en) * | 2008-12-16 | 2009-12-30 | 海南美大制药有限公司 | A kind of aluminum-magnesium silicate compound and synthetic method thereof |
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EP1422198A1 (en) * | 2001-07-27 | 2004-05-26 | Chiyoda Corporation | Porous 4 group metal oxide and method for preparation thereof |
CN1907567A (en) * | 2006-08-16 | 2007-02-07 | 天津化工研究设计院 | Forming method for porous composite metallic oxide catalytic carrier |
CN101613110A (en) * | 2008-12-16 | 2009-12-30 | 海南美大制药有限公司 | A kind of aluminum-magnesium silicate compound and synthetic method thereof |
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共沉淀法合成三硅酸镁及其微观分析;冯凌等;《北京科技大学学报》;20091231;第31卷(第2期);第1.1节 * |
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