CN1884082A - Method for preparing pseudo-boehmite with large pore volume and high specific surface area - Google Patents
Method for preparing pseudo-boehmite with large pore volume and high specific surface area Download PDFInfo
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- 238000000034 method Methods 0.000 title claims abstract description 39
- VXAUWWUXCIMFIM-UHFFFAOYSA-M aluminum;oxygen(2-);hydroxide Chemical compound [OH-].[O-2].[Al+3] VXAUWWUXCIMFIM-UHFFFAOYSA-M 0.000 title claims abstract description 36
- 239000011148 porous material Substances 0.000 title claims abstract description 26
- 238000000354 decomposition reaction Methods 0.000 claims abstract description 60
- ANBBXQWFNXMHLD-UHFFFAOYSA-N aluminum;sodium;oxygen(2-) Chemical compound [O-2].[O-2].[Na+].[Al+3] ANBBXQWFNXMHLD-UHFFFAOYSA-N 0.000 claims abstract description 47
- 229910001388 sodium aluminate Inorganic materials 0.000 claims abstract description 47
- 239000013078 crystal Substances 0.000 claims abstract description 38
- 239000000843 powder Substances 0.000 claims abstract description 29
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 claims abstract description 13
- 230000007935 neutral effect Effects 0.000 claims abstract description 10
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 7
- 238000001816 cooling Methods 0.000 claims abstract 2
- 239000000047 product Substances 0.000 claims description 23
- 239000012065 filter cake Substances 0.000 claims description 11
- 238000004519 manufacturing process Methods 0.000 claims description 9
- 238000002360 preparation method Methods 0.000 claims description 9
- 238000005406 washing Methods 0.000 claims description 7
- 238000001035 drying Methods 0.000 claims description 5
- 238000006243 chemical reaction Methods 0.000 claims description 2
- 230000035484 reaction time Effects 0.000 claims description 2
- 230000015556 catabolic process Effects 0.000 claims 2
- 238000006731 degradation reaction Methods 0.000 claims 2
- 238000010981 drying operation Methods 0.000 claims 1
- 238000003828 vacuum filtration Methods 0.000 claims 1
- 229910018072 Al 2 O 3 Inorganic materials 0.000 abstract description 20
- 230000000694 effects Effects 0.000 abstract description 3
- 239000000203 mixture Substances 0.000 abstract description 3
- 238000004064 recycling Methods 0.000 abstract description 2
- 229910001593 boehmite Inorganic materials 0.000 description 12
- FAHBNUUHRFUEAI-UHFFFAOYSA-M hydroxidooxidoaluminium Chemical compound O[Al]=O FAHBNUUHRFUEAI-UHFFFAOYSA-M 0.000 description 12
- 239000003518 caustics Substances 0.000 description 11
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 description 9
- 238000005516 engineering process Methods 0.000 description 4
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 3
- 229910052782 aluminium Inorganic materials 0.000 description 3
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 3
- 229910001679 gibbsite Inorganic materials 0.000 description 3
- 238000004131 Bayer process Methods 0.000 description 2
- AMQJEAYHLZJPGS-UHFFFAOYSA-N N-Pentanol Chemical compound CCCCCO AMQJEAYHLZJPGS-UHFFFAOYSA-N 0.000 description 2
- 229910001570 bauxite Inorganic materials 0.000 description 2
- 238000001354 calcination Methods 0.000 description 2
- 239000003054 catalyst Substances 0.000 description 2
- 238000006555 catalytic reaction Methods 0.000 description 2
- 238000004090 dissolution Methods 0.000 description 2
- 238000002474 experimental method Methods 0.000 description 2
- 239000000706 filtrate Substances 0.000 description 2
- ZSIAUFGUXNUGDI-UHFFFAOYSA-N hexan-1-ol Chemical compound CCCCCCO ZSIAUFGUXNUGDI-UHFFFAOYSA-N 0.000 description 2
- 229910052751 metal Inorganic materials 0.000 description 2
- 239000002184 metal Substances 0.000 description 2
- 150000002739 metals Chemical class 0.000 description 2
- 239000002243 precursor Substances 0.000 description 2
- 239000011734 sodium Substances 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- 229910006636 γ-AlOOH Inorganic materials 0.000 description 2
- 229910018626 Al(OH) Inorganic materials 0.000 description 1
- 241000640882 Condea Species 0.000 description 1
- MXRIRQGCELJRSN-UHFFFAOYSA-N O.O.O.[Al] Chemical compound O.O.O.[Al] MXRIRQGCELJRSN-UHFFFAOYSA-N 0.000 description 1
- 239000003463 adsorbent Substances 0.000 description 1
- 238000005054 agglomeration Methods 0.000 description 1
- 230000002776 aggregation Effects 0.000 description 1
- 150000001298 alcohols Chemical class 0.000 description 1
- -1 aluminum hydroxide-aluminum oxide-aluminum-aluminum Chemical compound 0.000 description 1
- 239000000969 carrier Substances 0.000 description 1
- 230000000295 complement effect Effects 0.000 description 1
- 230000001276 controlling effect Effects 0.000 description 1
- 230000002596 correlated effect Effects 0.000 description 1
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- 229910052593 corundum Inorganic materials 0.000 description 1
- 238000002425 crystallisation Methods 0.000 description 1
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- 230000007547 defect Effects 0.000 description 1
- 238000001514 detection method Methods 0.000 description 1
- 239000006185 dispersion Substances 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 238000010335 hydrothermal treatment Methods 0.000 description 1
- 229910052500 inorganic mineral Inorganic materials 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 239000011707 mineral Substances 0.000 description 1
- 239000003960 organic solvent Substances 0.000 description 1
- 238000001556 precipitation Methods 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
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- 229910001845 yogo sapphire Inorganic materials 0.000 description 1
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Abstract
本发明是一种大孔容、高比表面拟薄水铝石的制备方法,其步骤有:先将SB粉加入到含有110~200g/L-Al2O3和苛化系数为1.30~1.75的铝酸钠溶液中,晶种的加入量和溶液中Al2O3的质量比恒为1.0,随后在100~150℃的水热条件下分解3~16小时;抽滤冷却后的分解产物,水洗至中性,再经乙醇洗涤和干燥后,即可得到单相拟薄水铝石。本发明采用的SB粉晶种活性高,水热稳定性好,可以在很低的晶种比和较短的分解时间内得到较高的溶液分解率。本方法具有工艺简单、条件温和、晶种可连续循环使用和可操作性强等优点,为从廉价的铝酸钠溶液制备高附加值拟薄水铝石提供了一种新的可供选择的路径。The present invention is a method for preparing pseudo-boehmite with large pore volume and high specific surface area. The steps include: firstly adding SB powder to a mixture containing 110-200g/L-Al 2 O 3 and a causticization coefficient of 1.30-1.75 In the sodium aluminate solution, the mass ratio of the amount of seed crystals added to the Al 2 O 3 in the solution is 1.0, and then it is decomposed under the hydrothermal condition of 100-150 ℃ for 3-16 hours; the decomposed product after cooling is suction filtered , washed with water until neutral, then washed with ethanol and dried to obtain single-phase pseudo-boehmite. The SB powder seed crystal adopted in the invention has high activity and good hydrothermal stability, and can obtain a higher solution decomposition rate at a very low seed crystal ratio and a short decomposition time. The method has the advantages of simple process, mild conditions, continuous recycling of seed crystals and strong operability, and provides a new alternative for preparing high value-added pseudo-boehmite from cheap sodium aluminate solution. path.
Description
技术领域technical field
本发明涉及拟薄水铝石的制备,尤其涉及一种以SB粉为晶种,水热分解铝酸钠溶液制备大孔容、高比表面拟薄水铝石的方法。The invention relates to the preparation of pseudo-boehmite, in particular to a method for preparing pseudo-boehmite with large pore volume and high specific surface area by hydrothermally decomposing sodium aluminate solution with SB powder as crystal seed.
背景技术Background technique
拟薄水铝石(pseudoboehmite)是一种组成不确定、结晶不完整、因而性能可控的化学品氧化铝,化学式为γ-AlOOH·nH2O(n=0.08~0.62),其晶体结构和薄水铝石(γ-AlOOH)相似,典型结构为很薄的皱折片层。经拟薄水铝石焙烧得到的γ-Al2O3比表面较高,在石油化工领域广泛用作催化剂载体,而经薄水铝石焙烧得到的γ-Al2O3比表面较低,一般难以用于催化领域。Pseudoboehmite is a chemical alumina with uncertain composition, incomplete crystallization and controllable properties. Its chemical formula is γ-AlOOH·nH 2 O (n=0.08~0.62). Boehmite (γ-AlOOH) is similar, with a typical structure of very thin wrinkled sheets. The specific surface of γ-Al 2 O 3 obtained by calcination of pseudo-boehmite is higher, and it is widely used as a catalyst carrier in the field of petrochemical industry, while the specific surface of γ-Al 2 O 3 obtained by calcination of boehmite is lower. It is generally difficult to be used in the field of catalysis.
SB粉是德国Condea公司开发成功的一种以高纯铝旋屑和高级醇(正戊醇、正己醇)为原料生产的优质拟薄水铝石,SB粉由于晶型好、孔结构容易控制、比表面和纯度高,在催化领域被广为应用。其生产经历了氢氧化铝——氧化铝——铝——醇铝——氢氧化铝的循环过程。但该方法使用的有机溶剂存在毒性,生产成本也较高。而以拜尔法铝土矿溶出中间体——廉价的精制铝酸钠溶液为原料,采用铝酸钠溶液晶种分解技术,直接制取性能和SB粉相近的高质量拟薄水铝石,就有可能克服SB粉制造工艺的缺点。SB powder is a kind of high-quality pseudo-boehmite produced by high-purity aluminum rotary shavings and higher alcohols (n-pentanol, n-hexanol) successfully developed by German Condea company. SB powder is easy to control due to its good crystal form and pore structure. , specific surface and high purity, it is widely used in the field of catalysis. Its production has gone through the cycle process of aluminum hydroxide-aluminum oxide-aluminum-aluminum alcohol-aluminum hydroxide. However, the organic solvent used in this method is toxic and the production cost is relatively high. However, the Bayer process bauxite dissolution intermediate - cheap refined sodium aluminate solution is used as raw material, and the sodium aluminate solution seed crystal decomposition technology is used to directly produce high-quality pseudo-boehmite with properties similar to those of SB powder. It is possible to overcome the shortcomings of the SB powder manufacturing process.
铝酸钠溶液的晶种分解是冶金级氧化铝生产过程中的关键工序,传统晶种分解以添加三水铝石晶种和析出氢氧化铝(Al(OH)3)为基础,不仅分解时间长、分解率低,而且Al(OH)3转化成氧化铝的过程能耗高、产品质量难以调控。The seed crystal decomposition of sodium aluminate solution is a key process in the production process of metallurgical grade alumina. The traditional seed crystal decomposition is based on adding gibbsite seed crystals and precipitation of aluminum hydroxide (Al(OH) 3 ), not only the decomposition time Long, low decomposition rate, and the process of converting Al(OH) 3 into alumina has high energy consumption and difficult to control the product quality.
采用薄水铝石晶种分解铝酸钠溶液制备薄水铝石的方法已有报道。WO9,858,876公开了一种90℃下铝酸钠溶液分解制备薄水铝石的方法,晶种为三水铝石水热处理后得到的薄水铝石。在晶种比为1.76,铝酸钠溶液组成90.0g/L-Na2O、99g/L-Al2O3的条件下,分解96h时铝酸钠溶液的分解率为40.53%。该方法的主要缺点是分解时间过长,而且分解产物只能用作冶金级氧化铝的前驱物。A method for preparing boehmite by decomposing sodium aluminate solution with boehmite seeds has been reported. WO9,858,876 discloses a method for preparing boehmite by decomposing sodium aluminate solution at 90°C, the seed crystal is boehmite obtained after hydrothermal treatment of gibbsite. Under the condition that the seed crystal ratio is 1.76 and the composition of sodium aluminate solution is 90.0g/L-Na 2 O and 99g/L-Al 2 O 3 , the decomposition rate of sodium aluminate solution is 40.53% when decomposed for 96 hours. The main disadvantage of this method is that the decomposition time is too long, and the decomposition products can only be used as precursors of metallurgical grade alumina.
CN1186046A公开了一种先向铝酸钠溶液中通入CO2,待溶液的苛化系数αK降至1.20~1.30后,再用铝酸钠溶液晶种分解制备薄水铝石的方法。在铝酸钠溶液组成90~110g/L-Al2O3、苛化系数1.40~1.60、110~120℃和晶种比2.0~2.5的条件下分解30h时铝酸钠溶液的分解率为48~52%。该方法溶液中铝的利用率较高,但分解产物同样只能用作冶金级氧化铝的前驱物,通入CO2还消耗了后续工艺中利用价值较高的NaOH,主要操作参数范围过窄也不利于铝酸钠溶液分解过程的操作。CN1186046A discloses a method in which CO 2 is introduced into sodium aluminate solution first, and after the causticization coefficient α K of the solution is reduced to 1.20-1.30, the method of decomposing and preparing boehmite by seed crystals of sodium aluminate solution is disclosed. The decomposition rate of sodium aluminate solution is 48 when the sodium aluminate solution is decomposed for 30 hours under the conditions of 90~110g/L-Al 2 O 3 , caustic coefficient 1.40~1.60, 110~120℃ and seed ratio 2.0~2.5. ~52%. This method has a high utilization rate of aluminum in the solution, but the decomposition product can only be used as a precursor of metallurgical grade alumina, and the introduction of CO 2 also consumes NaOH with high utilization value in subsequent processes, and the range of main operating parameters is too narrow Also be unfavorable for the operation of sodium aluminate solution decomposition process.
CN1733607A公开了一种制备较高活性薄水铝石晶种及其分解铝酸钠溶液制备微米级薄水铝石的方法。该方法先在0~90℃、H2O2/Al2O3=3.0~7.0(摩尔比)下用8~30%的H2O2溶液沉淀含有50~250g/L-Al2O3、苛化系数αK为1.30~3.50的铝酸钠溶液,然后以依次经过滤、水洗、乙醇分散并洗涤以及干燥得到的薄水铝石为晶种,在铝酸钠溶液组成60~180g/L-Al2O3、苛化系数1.30~1.80和较低晶种比下分解,最高分解率可达50%以上。CN1733607A discloses a method for preparing relatively active boehmite seed crystals and decomposing sodium aluminate solution to prepare micron-sized boehmite. In this method, 8-30 % H 2 O 2 solution containing 50-250g/L-Al 2 O 3 A sodium aluminate solution with a caustic coefficient α K of 1.30 to 3.50, and then the boehmite obtained by filtering, washing with water, ethanol dispersion and washing and drying in sequence as the seed crystal, in the sodium aluminate solution to form 60 to 180g/ L-Al 2 O 3 , caustic coefficient 1.30-1.80 and low seed crystal ratio can be decomposed, and the highest decomposition rate can reach more than 50%.
有研究者[Filippou D,Paspaliafris I.Light Metals.New York:the Minerals,Metals & MaterialsSociety,1993.119]认为,在100~150℃之间薄水铝石是铝酸钠溶液分解所能得到的唯一分解产物,但如果采用特殊的分解技术,例如,加入一定量的醇降低水的活度,有可能得到拟薄水铝石。现有铝酸钠溶液晶种分解技术的缺陷是分解产物通常是三水铝石或薄水铝石等低附加值冶金级氧化铝产品。Some researchers [Filippou D, Paspaliafris I. Light Metals. New York: the Minerals, Metals & Materials Society, 1993.119] believe that boehmite is the only decomposition that can be obtained by decomposition of sodium aluminate solution between 100 and 150 °C products, but if a special decomposition technique is used, for example, adding a certain amount of alcohol to reduce the activity of water, it is possible to obtain pseudo-boehmite. The defect of the existing sodium aluminate solution seed crystal decomposition technology is that the decomposition products are usually low value-added metallurgical grade alumina products such as gibbsite or boehmite.
发明内容Contents of the invention
本发明所要解决的技术问题是:提供一种铝酸钠溶液水热晶种分解制备大孔容、高比表面拟薄水铝石的方法,该方法能够制备附加值较高的拟薄水铝石产品。The technical problem to be solved by the present invention is to provide a method for preparing pseudo-boehmite with large pore volume and high specific surface area by hydrothermal seed crystal decomposition of sodium aluminate solution, which can prepare pseudo-boehmite with higher added value stone products.
本发明解决其技术问题所采用的技术方案是:以SB粉为晶种,水热分解铝酸钠溶液制备大孔容、高比表面拟薄水铝石,具体步骤包括:The technical solution adopted by the present invention to solve the technical problem is: use SB powder as crystal seed, hydrothermally decompose sodium aluminate solution to prepare pseudo-boehmite with large pore volume and high specific surface area, and the specific steps include:
1.将SB粉作为晶种,加入到含有110~200g/L-Al2O3和苛化系数为1.30~1.75的铝酸钠溶液中进行分解,晶种的加入量和溶液中Al2O3的质量比为1∶1,随后在密闭水热条件下分解,得分解产物;1. Use SB powder as a seed crystal, add it to a sodium aluminate solution containing 110-200g/L-Al 2 O 3 and a caustic coefficient of 1.30-1.75 for decomposition, the amount of seed crystal added and the Al 2 O The mass ratio of 3 is 1:1, and then decomposed under closed hydrothermal conditions to obtain decomposition products;
2.分解产物经冷却、真空抽滤后,用水洗涤至中性,得中性滤饼;2. After the decomposition product is cooled and vacuum filtered, it is washed with water until neutral to obtain a neutral filter cake;
3.将中性滤饼用其2.0~4.0倍体积的乙醇分散并洗涤一次,经干燥工序后,即可得到单相拟薄水铝石;3. Disperse and wash the neutral filter cake once with 2.0 to 4.0 times the volume of ethanol, and after drying, single-phase pseudo-boehmite can be obtained;
4.步骤1中的分解产物也可以返回到前工序作为晶种,随后重复上述铝酸钠溶液水热晶种分解步骤。4. The decomposition product in step 1 can also be returned to the previous process as a seed crystal, and then the above-mentioned sodium aluminate solution hydrothermal seed crystal decomposition step is repeated.
本发明与现有拟薄水铝石的制备技术相比,具有以下主要优点:Compared with the preparation technology of existing pseudo-boehmite, the present invention has the following main advantages:
1.本方法采用的SB粉晶种具有很高的活性,该晶种水热分解铝酸钠溶液高效、经济,可以在很低的晶种比(SR=1.0)和分解时间(3h)内获得较高的溶液分解率,分解率最高可达30%以上;1. The SB powder seed crystal adopted in this method has very high activity, and the hydrothermal decomposition of the sodium aluminate solution by the seed crystal is efficient and economical, and can be performed within a very low seed crystal ratio (SR=1.0) and decomposition time (3h) Obtain a high solution decomposition rate, the decomposition rate can reach more than 30%;
2.本方法提供的SB粉水热分解铝酸钠溶液制备拟薄水铝石的方法不仅工艺简单,条件温和,晶种可以连续循环使用多次,而且产物的孔容大、比表面高,部分性质甚至超过了SB粉的技术指标,显示了其在石油化工等行业用作催化剂载体和吸附剂的潜在应用前景;2. The method for preparing pseudo-boehmite by hydrothermally decomposing sodium aluminate solution of SB powder provided by this method is not only simple in process, mild in condition, and the crystal seed can be continuously recycled for many times, and the product has large pore volume and high specific surface area. Some properties even exceed the technical indicators of SB powder, showing its potential application prospects as catalyst carriers and adsorbents in petrochemical and other industries;
3.本方法中SB粉水热分解铝酸钠溶液后,分解滤液的pH较分解前大为提高。和拜耳法等碱法生产冶金级氧化铝的过程相结合后,该分解滤液可以返回到碱法生产氧化铝过程中铝土矿的溶出阶段加以循环利用。3. After the SB powder hydrothermally decomposes the sodium aluminate solution in this method, the pH of the decomposed filtrate is greatly improved compared with that before the decomposition. After being combined with the process of producing metallurgical grade alumina by alkaline process such as Bayer process, the decomposed filtrate can be returned to the dissolution stage of bauxite in the process of producing alumina by alkaline process for recycling.
总之,本方法突破了拟薄水铝石的传统生产工艺,大大缩短了工艺流程,降低了生产成本,可望发展成为包括醇铝水解法在内的传统高附加值拟薄水铝石和γ-Al2O3制备技术的补充方法。In short, this method breaks through the traditional production process of pseudo-boehmite, greatly shortens the process flow, and reduces production costs. It is expected to develop into traditional high-value-added pseudo-boehmite and γ- Complementary approach to Al2O3 preparation technology.
附图说明Description of drawings
图1是实施例1~实施例4分解产物和SB粉的XRD图谱。Fig. 1 is the XRD spectrum of embodiment 1~embodiment 4 decomposition product and SB powder.
具体实施方式Detailed ways
本发明提供的是一种以SB粉为晶种,水热分解铝酸钠溶液制备大孔容、高比表面拟薄水铝石的方法,具体步骤包括:The present invention provides a method for preparing pseudo-boehmite with large pore volume and high specific surface area by hydrothermally decomposing sodium aluminate solution with SB powder as crystal seed, and the specific steps include:
1.将SB粉作为原始晶种,加入到铝酸钠溶液中进行分解,品种的加入量和溶液中Al2O3的质量比为1∶1,随后在密闭水热条件(反应温度100~150℃,反应时间3~16小时)下分解,得分解产物。该分解产物也可以返回到前工序作为晶种,以减少SB粉晶种的用量,降低生产成本。原始晶种的比表面积和孔容大小分别为227.2m2/g和0.40cm3/g左右。1. Use SB powder as the original crystal seed, add it to the sodium aluminate solution to decompose, the amount of the species added and the mass ratio of Al 2 O 3 in the solution are 1:1, and then under closed hydrothermal conditions (reaction temperature 100 ~ 150°C, reaction time 3 to 16 hours) to decompose and obtain decomposition products. The decomposition product can also be returned to the previous process as a seed crystal to reduce the amount of SB powder seed crystals and reduce production costs. The specific surface area and pore volume of the original seed crystals are about 227.2m 2 /g and 0.40cm 3 /g respectively.
上述分解条件的控制很关键。The control of the above decomposition conditions is critical.
应该控制铝酸钠溶液中的Al2O3浓度在110~200g/L-Al2O3和苛化系数在1.30~1.75之间,以保证较高的铝酸钠溶液分解率,并降低后续工艺脱除Na+的难度。若溶液中的Al2O3浓度为200g/L,则溶液的苛化系数应为1.30;若溶液中的Al2O3浓度为110g/L,则溶液的苛化系数应为1.75。若溶液中的Al2O3浓度处于110g/L至200g/L之间时,则溶液的苛化系数也应处于1.75至1.30之间。总之,选择铝酸钠溶液中的Al2O3浓度和苛化系数应成负相关关系。The concentration of Al 2 O 3 in the sodium aluminate solution should be controlled between 110-200g/L-Al 2 O 3 and the caustic coefficient between 1.30-1.75 to ensure a higher decomposition rate of the sodium aluminate solution and reduce the subsequent The difficulty of removing Na + by process. If the concentration of Al 2 O 3 in the solution is 200g/L, the causticization coefficient of the solution should be 1.30; if the concentration of Al 2 O 3 in the solution is 110g/L, the causticization coefficient of the solution should be 1.75. If the concentration of Al 2 O 3 in the solution is between 110g/L and 200g/L, the caustic coefficient of the solution should also be between 1.75 and 1.30. In short, the concentration of Al 2 O 3 in the sodium aluminate solution and the caustic coefficient should be negatively correlated.
SB粉分解铝酸钠溶液时,通过控制不同水热分解温度下的分解时间,使溶液中的铝以大孔容、高比表面的拟薄水铝石形式析出。100℃下铝酸钠溶液水热分解的时间不少于16h,125℃下铝酸钠溶液水热分解的时间不少于3h。而分解铝酸钠溶液的温度处于100℃至125℃之间时,相应水热分解的时间也应处于16h至3h之间。总之,选择的水热分解温度和水热分解时间之间应成负相关关系。When SB powder decomposes sodium aluminate solution, by controlling the decomposition time at different hydrothermal decomposition temperatures, the aluminum in the solution is precipitated in the form of pseudo-boehmite with large pore volume and high specific surface area. The hydrothermal decomposition time of sodium aluminate solution at 100°C is not less than 16h, and the hydrothermal decomposition time of sodium aluminate solution at 125°C is not less than 3h. When the temperature for decomposing the sodium aluminate solution is between 100°C and 125°C, the corresponding hydrothermal decomposition time should also be between 16h and 3h. In conclusion, there should be a negative correlation between the selected hydrothermal decomposition temperature and hydrothermal decomposition time.
2.分解产物经冷却、真空抽滤后,用水洗涤至中性,得中性滤饼。2. After the decomposition product is cooled and vacuum filtered, it is washed with water until neutral to obtain a neutral filter cake.
3.将中性滤饼用其2.0~4.0倍体积的乙醇分散并洗涤一次,随后在100~120℃下普通干燥10~12h,即可得到比表面积为176.8~213.6m2/g和孔容大小为0.59~0.86cm3/g的单相拟薄水铝石。3. Disperse and wash the neutral filter cake with 2.0-4.0 times the volume of ethanol, and then dry it at 100-120°C for 10-12 hours to obtain a specific surface area of 176.8-213.6m 2 /g and a pore volume Single-phase pseudo-boehmite with a size of 0.59-0.86 cm 3 /g.
该步骤中,用乙醇洗涤中性滤饼,主要是为了能够有效地消除洗涤产物在后续干燥过程中因富含湿存水而出现的硬团聚,导致分解产物的孔容和比表面下降。In this step, the neutral filter cake is washed with ethanol, mainly to effectively eliminate the hard agglomeration of the washed product due to the rich wet water in the subsequent drying process, resulting in a decrease in the pore volume and specific surface of the decomposition product.
下面结合几个具体实施例对本发明作进一步说明。The present invention will be further described below in conjunction with several specific examples.
实施例1:将一定量SB粉加入到含有140g/L-Al2O3、苛化系数αK为1.30的40ml铝酸钠溶液中,SB粉的加入量与铝酸钠溶液中Al2O3的重量比为1∶1,125℃下连续水热分解3h,分解率为31.7%;分解产物经冷却、真空抽滤、去离子水洗涤至中性后,用2倍于固体体积的乙醇分散并洗涤,滤饼在100℃下干燥12h后,干燥产物经XRD检测为100%的拟薄水铝石,采用全自动比表面及孔隙度分析仪测定的其比表面积和孔容大小分别为176.8m2/g和0.59cm3/g。Example 1: A certain amount of SB powder is added to 40ml of sodium aluminate solution containing 140g/L-Al 2 O 3 and the caustic coefficient α K is 1.30 . The weight ratio of 3 is 1:1, continuous hydrothermal decomposition at 125°C for 3 hours, and the decomposition rate is 31.7%. After dispersing and washing, the filter cake was dried at 100°C for 12 hours, and the dried product was detected by XRD as 100% pseudo-boehmite. The specific surface area and pore volume measured by the automatic specific surface and porosity analyzer were respectively 176.8m 2 /g and 0.59cm 3 /g.
实施例2:将一定量SB粉加入到含有110g/L-Al2O3、苛化系数αK为1.75的40ml铝酸钠溶液中,SB粉的加入量与铝酸钠溶液中Al2O3的重量比为1∶1,100℃下连续水热分解16h,分解率为16.2%;分解产物经冷却、真空抽滤、去离子水洗涤至中性后,用4倍于固体体积的乙醇分散并洗涤,滤饼在120℃下干燥10h后,干燥产物经XRD检测为100%的拟薄水铝石,采用全自动比表面及孔隙度分析仪测定的其比表面和孔容大小分别为195.2m2/g和0.86cm3/g。Example 2: A certain amount of SB powder is added to 40ml of sodium aluminate solution containing 110g/L-Al 2 O 3 and the caustic coefficient α K is 1.75. The amount of SB powder added is the same as that of Al 2 O in sodium aluminate solution The weight ratio of 3 is 1:1, continuous hydrothermal decomposition at 100°C for 16 hours, and the decomposition rate is 16.2%. After dispersing and washing, the filter cake was dried at 120°C for 10 hours, and the dried product was detected by XRD as 100% pseudo-boehmite. The specific surface and pore volume measured by the automatic specific surface and porosity analyzer were respectively 195.2 m 2 /g and 0.86 cm 3 /g.
实施例3:将一定量SB粉加入到含有200g/L-Al2O3、苛化系数αK为1.30的40ml铝酸钠溶液中,SB粉的加入量与铝酸钠溶液中Al2O3的重量比为1∶1,150℃下连续水热分解9h,分解率为23.1%;分解产物经冷却、真空抽滤、去离子水洗涤至中性后,用2倍于固体体积的乙醇分散并洗涤,滤饼在110℃下干燥11h后,干燥产物经XRD检测为100%的拟薄水铝石,采用全自动比表面及孔隙度分析仪测定的其比表面和孔容大小分别为181.3m2/g和0.78cm3/g。Example 3: A certain amount of SB powder is added to 40ml of sodium aluminate solution containing 200g/L-Al 2 O 3 and the caustic coefficient α K is 1.30. The amount of SB powder added is the same as that of Al 2 O in sodium aluminate solution The weight ratio of 3 is 1:1, continuous hydrothermal decomposition at 150°C for 9 hours, and the decomposition rate is 23.1%. After dispersing and washing, the filter cake was dried at 110°C for 11 hours, and the dried product was detected by XRD as 100% pseudo-boehmite. The specific surface and pore volume measured by the automatic specific surface and porosity analyzer were respectively 181.3m 2 /g and 0.78cm 3 /g.
实施例4:将一定量SB粉加入到含有140g/L-Al2O3、苛化系数αK为1.45的40ml铝酸钠溶液中,SB粉的加入量与铝酸钠溶液中Al2O3的重量比为1∶1,125℃下连续水热分解3h,分解率为22.1%;分解产物经冷却、真空抽滤、去离子水洗涤至中性后,用3倍于固体体积的乙醇分散并洗涤,滤饼在100℃下干燥12h后,干燥产物经XRD检测为100%的拟薄水铝石,其比表面和孔容分别为182.5m2/g和0.64cm3/g。采取和上述方法相同的步骤,每次循环水热分解铝酸钠溶液实验采用的晶种均为前一次分解实验的分解产物,连续水热分解3次后,分解率为21.8%,干燥产物经XRD检测为100%的拟薄水铝石,其比表面和孔容分别为213.6m2/g和0.84cm3/g。Example 4: A certain amount of SB powder is added to 40ml of sodium aluminate solution containing 140g/L-Al 2 O 3 and the caustic coefficient α K is 1.45. The amount of SB powder added is the same as that of Al 2 O in sodium aluminate solution The weight ratio of 3 is 1:1, continuous hydrothermal decomposition at 125°C for 3 hours, and the decomposition rate is 22.1%. After dispersing and washing, the filter cake was dried at 100°C for 12 hours, and the dried product was detected by XRD to be 100% pseudo-boehmite, and its specific surface and pore volume were 182.5m 2 /g and 0.64cm 3 /g, respectively. Take the same steps as the above-mentioned method. The seeds used in each cycle of hydrothermal decomposition of sodium aluminate solution experiments are the decomposition products of the previous decomposition experiment. After continuous hydrothermal decomposition for 3 times, the decomposition rate is 21.8%. The XRD detection is 100% pseudo-boehmite, and its specific surface and pore volume are 213.6m 2 /g and 0.84cm 3 /g, respectively.
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