CN102008939A - Method for preparing aluminum-manganese composite oxide modified molecular sieve - Google Patents
Method for preparing aluminum-manganese composite oxide modified molecular sieve Download PDFInfo
- Publication number
- CN102008939A CN102008939A CN 201010543259 CN201010543259A CN102008939A CN 102008939 A CN102008939 A CN 102008939A CN 201010543259 CN201010543259 CN 201010543259 CN 201010543259 A CN201010543259 A CN 201010543259A CN 102008939 A CN102008939 A CN 102008939A
- Authority
- CN
- China
- Prior art keywords
- manganese
- composite oxide
- aluminium
- preparation
- solution
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Granted
Links
- URGAHOPLAPQHLN-UHFFFAOYSA-N sodium aluminosilicate Chemical class [Na+].[Al+3].[O-][Si]([O-])=O.[O-][Si]([O-])=O URGAHOPLAPQHLN-UHFFFAOYSA-N 0.000 title claims abstract description 54
- -1 aluminum-manganese Chemical compound 0.000 title claims abstract description 48
- 239000002131 composite material Substances 0.000 title claims abstract description 42
- 238000000034 method Methods 0.000 title abstract description 11
- 239000002808 molecular sieve Substances 0.000 claims abstract description 39
- 239000000243 solution Substances 0.000 claims abstract description 31
- 238000003756 stirring Methods 0.000 claims abstract description 24
- 150000002696 manganese Chemical class 0.000 claims abstract description 17
- 239000011259 mixed solution Substances 0.000 claims abstract description 17
- 239000007800 oxidant agent Substances 0.000 claims abstract description 17
- 230000001590 oxidative effect Effects 0.000 claims abstract description 16
- 230000032683 aging Effects 0.000 claims abstract description 11
- AZDRQVAHHNSJOQ-UHFFFAOYSA-N alumane Chemical class [AlH3] AZDRQVAHHNSJOQ-UHFFFAOYSA-N 0.000 claims abstract description 7
- 238000005406 washing Methods 0.000 claims abstract description 6
- 238000006243 chemical reaction Methods 0.000 claims abstract description 3
- 238000001035 drying Methods 0.000 claims abstract description 3
- 239000003513 alkali Substances 0.000 claims abstract 2
- HEMHJVSKTPXQMS-UHFFFAOYSA-M sodium hydroxide Inorganic materials [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 claims description 33
- 238000002360 preparation method Methods 0.000 claims description 26
- 239000000203 mixture Substances 0.000 claims description 12
- KWYUFKZDYYNOTN-UHFFFAOYSA-M Potassium hydroxide Chemical compound [OH-].[K+] KWYUFKZDYYNOTN-UHFFFAOYSA-M 0.000 claims description 9
- 239000002245 particle Substances 0.000 claims description 9
- VSCWAEJMTAWNJL-UHFFFAOYSA-K aluminium trichloride Chemical compound Cl[Al](Cl)Cl VSCWAEJMTAWNJL-UHFFFAOYSA-K 0.000 claims description 8
- CDBYLPFSWZWCQE-UHFFFAOYSA-L Sodium Carbonate Chemical compound [Na+].[Na+].[O-]C([O-])=O CDBYLPFSWZWCQE-UHFFFAOYSA-L 0.000 claims description 6
- MHAJPDPJQMAIIY-UHFFFAOYSA-N Hydrogen peroxide Chemical compound OO MHAJPDPJQMAIIY-UHFFFAOYSA-N 0.000 claims description 5
- 229910021380 Manganese Chloride Inorganic materials 0.000 claims description 5
- GLFNIEUTAYBVOC-UHFFFAOYSA-L Manganese chloride Chemical compound Cl[Mn]Cl GLFNIEUTAYBVOC-UHFFFAOYSA-L 0.000 claims description 5
- 239000011565 manganese chloride Substances 0.000 claims description 5
- 235000002867 manganese chloride Nutrition 0.000 claims description 5
- 229940099607 manganese chloride Drugs 0.000 claims description 5
- WQYVRQLZKVEZGA-UHFFFAOYSA-N hypochlorite Chemical compound Cl[O-] WQYVRQLZKVEZGA-UHFFFAOYSA-N 0.000 claims description 4
- 229940099596 manganese sulfate Drugs 0.000 claims description 4
- 239000011702 manganese sulphate Substances 0.000 claims description 4
- 235000007079 manganese sulphate Nutrition 0.000 claims description 4
- SQQMAOCOWKFBNP-UHFFFAOYSA-L manganese(II) sulfate Chemical compound [Mn+2].[O-]S([O-])(=O)=O SQQMAOCOWKFBNP-UHFFFAOYSA-L 0.000 claims description 4
- KZBUYRJDOAKODT-UHFFFAOYSA-N Chlorine Chemical compound ClCl KZBUYRJDOAKODT-UHFFFAOYSA-N 0.000 claims description 3
- QAOWNCQODCNURD-UHFFFAOYSA-L Sulfate Chemical compound [O-]S([O-])(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-L 0.000 claims description 3
- 229940037003 alum Drugs 0.000 claims description 3
- 229910052782 aluminium Inorganic materials 0.000 claims description 3
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 claims description 3
- DIZPMCHEQGEION-UHFFFAOYSA-H aluminium sulfate (anhydrous) Chemical compound [Al+3].[Al+3].[O-]S([O-])(=O)=O.[O-]S([O-])(=O)=O.[O-]S([O-])(=O)=O DIZPMCHEQGEION-UHFFFAOYSA-H 0.000 claims description 3
- 239000011572 manganese Substances 0.000 claims description 3
- 229910052748 manganese Inorganic materials 0.000 claims description 3
- MIVBAHRSNUNMPP-UHFFFAOYSA-N manganese(2+);dinitrate Chemical compound [Mn+2].[O-][N+]([O-])=O.[O-][N+]([O-])=O MIVBAHRSNUNMPP-UHFFFAOYSA-N 0.000 claims description 3
- 239000011159 matrix material Substances 0.000 claims description 3
- BWHMMNNQKKPAPP-UHFFFAOYSA-L potassium carbonate Substances [K+].[K+].[O-]C([O-])=O BWHMMNNQKKPAPP-UHFFFAOYSA-L 0.000 claims description 3
- 239000012266 salt solution Substances 0.000 claims description 3
- 229910000029 sodium carbonate Inorganic materials 0.000 claims description 3
- PWHULOQIROXLJO-UHFFFAOYSA-N Manganese Chemical compound [Mn] PWHULOQIROXLJO-UHFFFAOYSA-N 0.000 claims description 2
- 230000035484 reaction time Effects 0.000 claims description 2
- 159000000013 aluminium salts Chemical class 0.000 claims 3
- 229910000329 aluminium sulfate Inorganic materials 0.000 claims 3
- 239000004411 aluminium Substances 0.000 claims 1
- 230000029087 digestion Effects 0.000 claims 1
- 230000010355 oscillation Effects 0.000 claims 1
- 229940072033 potash Drugs 0.000 claims 1
- 235000015320 potassium carbonate Nutrition 0.000 claims 1
- 238000010792 warming Methods 0.000 claims 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 abstract description 32
- 239000003463 adsorbent Substances 0.000 description 32
- 229910052785 arsenic Inorganic materials 0.000 description 24
- RQNWIZPPADIBDY-UHFFFAOYSA-N arsenic atom Chemical compound [As] RQNWIZPPADIBDY-UHFFFAOYSA-N 0.000 description 24
- 238000001179 sorption measurement Methods 0.000 description 15
- 239000008367 deionised water Substances 0.000 description 9
- 229910021641 deionized water Inorganic materials 0.000 description 9
- 239000007788 liquid Substances 0.000 description 7
- 238000001914 filtration Methods 0.000 description 6
- 239000000463 material Substances 0.000 description 6
- 239000007787 solid Substances 0.000 description 6
- 239000006228 supernatant Substances 0.000 description 6
- 229910018131 Al-Mn Inorganic materials 0.000 description 5
- 229910018461 Al—Mn Inorganic materials 0.000 description 5
- NUJOXMJBOLGQSY-UHFFFAOYSA-N manganese dioxide Chemical compound O=[Mn]=O NUJOXMJBOLGQSY-UHFFFAOYSA-N 0.000 description 4
- 230000007935 neutral effect Effects 0.000 description 4
- 238000011160 research Methods 0.000 description 3
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 2
- VEXZGXHMUGYJMC-UHFFFAOYSA-M Chloride anion Chemical compound [Cl-] VEXZGXHMUGYJMC-UHFFFAOYSA-M 0.000 description 2
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 2
- 239000005708 Sodium hypochlorite Substances 0.000 description 2
- GWEVSGVZZGPLCZ-UHFFFAOYSA-N Titan oxide Chemical compound O=[Ti]=O GWEVSGVZZGPLCZ-UHFFFAOYSA-N 0.000 description 2
- 239000002253 acid Substances 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 239000003344 environmental pollutant Substances 0.000 description 2
- 238000011049 filling Methods 0.000 description 2
- 230000003647 oxidation Effects 0.000 description 2
- 238000007254 oxidation reaction Methods 0.000 description 2
- TWNQGVIAIRXVLR-UHFFFAOYSA-N oxo(oxoalumanyloxy)alumane Chemical compound O=[Al]O[Al]=O TWNQGVIAIRXVLR-UHFFFAOYSA-N 0.000 description 2
- 231100000719 pollutant Toxicity 0.000 description 2
- 239000012286 potassium permanganate Substances 0.000 description 2
- SUKJFIGYRHOWBL-UHFFFAOYSA-N sodium hypochlorite Chemical compound [Na+].Cl[O-] SUKJFIGYRHOWBL-UHFFFAOYSA-N 0.000 description 2
- 239000002351 wastewater Substances 0.000 description 2
- 206010005003 Bladder cancer Diseases 0.000 description 1
- 206010007269 Carcinogenicity Diseases 0.000 description 1
- 208000008839 Kidney Neoplasms Diseases 0.000 description 1
- 206010058467 Lung neoplasm malignant Diseases 0.000 description 1
- 206010038389 Renal cancer Diseases 0.000 description 1
- 208000000453 Skin Neoplasms Diseases 0.000 description 1
- 208000007097 Urinary Bladder Neoplasms Diseases 0.000 description 1
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 description 1
- 229910000323 aluminium silicate Inorganic materials 0.000 description 1
- WGGGPNUBZBMKFR-UHFFFAOYSA-N aluminum manganese(2+) oxygen(2-) Chemical compound [O-2].[Al+3].[Mn+2] WGGGPNUBZBMKFR-UHFFFAOYSA-N 0.000 description 1
- 239000006227 byproduct Substances 0.000 description 1
- 231100000260 carcinogenicity Toxicity 0.000 description 1
- 230000007670 carcinogenicity Effects 0.000 description 1
- 230000015271 coagulation Effects 0.000 description 1
- 238000005345 coagulation Methods 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 230000018109 developmental process Effects 0.000 description 1
- 239000003651 drinking water Substances 0.000 description 1
- 235000020188 drinking water Nutrition 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
- 239000011521 glass Substances 0.000 description 1
- 238000011065 in-situ storage Methods 0.000 description 1
- 238000005342 ion exchange Methods 0.000 description 1
- 229910052742 iron Inorganic materials 0.000 description 1
- DALUDRGQOYMVLD-UHFFFAOYSA-N iron manganese Chemical compound [Mn].[Fe] DALUDRGQOYMVLD-UHFFFAOYSA-N 0.000 description 1
- 201000010982 kidney cancer Diseases 0.000 description 1
- 201000005202 lung cancer Diseases 0.000 description 1
- 208000020816 lung neoplasm Diseases 0.000 description 1
- 229910001437 manganese ion Inorganic materials 0.000 description 1
- 239000012528 membrane Substances 0.000 description 1
- 229910044991 metal oxide Inorganic materials 0.000 description 1
- 150000004706 metal oxides Chemical class 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 229910000027 potassium carbonate Inorganic materials 0.000 description 1
- TYJJADVDDVDEDZ-UHFFFAOYSA-M potassium hydrogencarbonate Chemical compound [K+].OC([O-])=O TYJJADVDDVDEDZ-UHFFFAOYSA-M 0.000 description 1
- SATVIFGJTRRDQU-UHFFFAOYSA-N potassium hypochlorite Chemical compound [K+].Cl[O-] SATVIFGJTRRDQU-UHFFFAOYSA-N 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- 230000008929 regeneration Effects 0.000 description 1
- 238000011069 regeneration method Methods 0.000 description 1
- 238000012827 research and development Methods 0.000 description 1
- 239000004576 sand Substances 0.000 description 1
- 229910052710 silicon Inorganic materials 0.000 description 1
- 239000010703 silicon Substances 0.000 description 1
- 201000000849 skin cancer Diseases 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 239000004408 titanium dioxide Substances 0.000 description 1
- 231100000331 toxic Toxicity 0.000 description 1
- 230000002588 toxic effect Effects 0.000 description 1
- 231100000419 toxicity Toxicity 0.000 description 1
- 230000001988 toxicity Effects 0.000 description 1
- 201000005112 urinary bladder cancer Diseases 0.000 description 1
Landscapes
- Solid-Sorbent Or Filter-Aiding Compositions (AREA)
Abstract
Description
技术领域technical field
本发明涉及一种用于去除水中砷污染物的、具有高比表面积及优良吸附性能的铝锰复合氧化物改性分子筛吸附剂的制备方法及在水处理应用中的使用方法。本发明属于水处理应用技术领域。The invention relates to a preparation method of an aluminum-manganese composite oxide modified molecular sieve adsorbent used for removing arsenic pollutants in water, having a high specific surface area and excellent adsorption performance, and a method for using it in water treatment applications. The invention belongs to the technical field of water treatment application.
背景技术Background technique
砷元素在自然界中普遍存在,因其具有剧毒和强致癌性而受到普遍关注。无机砷包括三价砷As(III)和五价砷As(V),且As(III)的危害远强于As(V),毒性可达到后者的60倍以上。长期饮用含砷水将会增加患膀胱癌、肺癌、肾癌和皮肤癌的危险,世界卫生组织(WHO)也将饮用水中的As的新标准定为10μg/L,因此如何去除并控制饮用水中的砷是目前国内外研究热点。Arsenic element is ubiquitous in nature and has attracted widespread attention because of its highly toxic and strong carcinogenicity. Inorganic arsenic includes trivalent arsenic As(III) and pentavalent arsenic As(V), and As(III) is far more harmful than As(V), and its toxicity can reach more than 60 times that of the latter. Drinking water containing arsenic for a long time will increase the risk of bladder cancer, lung cancer, kidney cancer and skin cancer. Arsenic in water is a research hotspot at home and abroad.
与其它的除砷方法如混凝法、离子交换法及膜处理等相比较起来,吸附法因其具有简便、经济、可再生等优点而得到广泛应用于处理砷浓度较低的水处理体系。但目前常用的除砷吸附剂中,如活性氧化铝、活性炭,通常仅对As(V)具有良好吸附能力,但对As(III)的去除能力较差。而加入预氧化不仅增长了处理成本和操作难度,还可能会产生对人体健康具有潜在危害的副产物。另一方面,根据最近国内外文献的报道,成本低廉的材料通常对砷的吸附容量较小,如载铁砂、天然铁锰矿石等;而具有较高吸附容量的材料往往成本过高,如二氧化钛。这也限制了除砷吸附材料的推广应用。因此,研究开发成本低廉、且对As(III)和As(V)均具有优良去除效果的新型吸附材料是目前国内外研究和技术开发的热点和难点问题。Compared with other arsenic removal methods such as coagulation method, ion exchange method and membrane treatment, adsorption method has been widely used in water treatment systems with low arsenic concentration because of its advantages of simplicity, economy and renewability. However, currently commonly used adsorbents for arsenic removal, such as activated alumina and activated carbon, usually only have good adsorption capacity for As(V), but poor removal capacity for As(III). The addition of pre-oxidation not only increases the processing cost and operational difficulty, but also may produce by-products that are potentially harmful to human health. On the other hand, according to recent domestic and foreign literature reports, low-cost materials usually have a small adsorption capacity for arsenic, such as iron-loaded sand, natural iron-manganese ore, etc.; while materials with high adsorption capacity are often too expensive, such as titanium dioxide . This also limits the popularization and application of arsenic removal adsorption materials. Therefore, the research and development of new adsorption materials with low cost and excellent removal effect on both As(III) and As(V) is a hot and difficult issue in research and technology development at home and abroad.
铝氧化物对As(V)有良好的去除能力,但却难以去除As(III)。二氧化锰对As(III)有很好的氧化性能,但对As(V)的吸附容量却较低。Aluminum oxide has good removal ability for As(V), but it is difficult to remove As(III). Manganese dioxide has good oxidation performance for As(III), but low adsorption capacity for As(V).
分子筛是一种具有立方晶格的硅铝酸盐化合物,主要由硅铝通过氧桥连接主城空旷的骨架结构,在结构中有很多孔径均匀的孔道和排列整齐、内表面积很大的空穴。分子筛具有低流体阻力,高吸附速度,吸附容量大,选择性强,机械强度高等优点,但单纯的分子筛对砷并不具有高选择性。Molecular sieve is a kind of aluminosilicate compound with cubic lattice. It is mainly composed of silicon and aluminum through oxygen bridges to connect the main city with an empty skeleton structure. . Molecular sieves have the advantages of low fluid resistance, high adsorption speed, large adsorption capacity, strong selectivity, and high mechanical strength, but simple molecular sieves do not have high selectivity for arsenic.
因此,如何有效地将铝氧化物和二氧化锰的化学特性结合起来,并利用分子筛的结构特性来同步去除As(III)/As(V),成为一个有待研究的课题。目前,使用铝锰复合氧化物改性分子筛去除水中砷的研究和应用未见文献报道和专利公开。Therefore, how to effectively combine the chemical properties of aluminum oxide and manganese dioxide and use the structural properties of molecular sieves to simultaneously remove As(III)/As(V) has become a subject to be studied. At present, there are no literature reports and patent publications on the research and application of using aluminum-manganese composite oxides to modify molecular sieves to remove arsenic in water.
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除砷污染物的吸附剂-铝锰复合氧化物改性分子筛的制备方法,以及该吸附剂在水处理中的使用方法。本发明涉及的吸附材料中,具有多孔结构的分子筛为负载基体,而铝锰复合金属氧化物则为吸附的主体部分。本发明涉及的吸附材料对As(III)和As(V)均具有广谱的优良吸附效能。The technical problem to be solved by the present invention is to provide a method for preparing an adsorbent for removing arsenic pollutants-aluminum-manganese composite oxide modified molecular sieve, and a method for using the adsorbent in water treatment. In the adsorption material involved in the present invention, the molecular sieve with a porous structure is the supporting matrix, and the aluminum-manganese composite metal oxide is the main part of the adsorption. The adsorption material involved in the invention has excellent adsorption efficiency with broad spectrum for both As(III) and As(V).
本发明的技术方案:Technical scheme of the present invention:
一种铝锰复合氧化物改性分子筛的制备方法,配制铝盐与锰盐的混合溶液,在均匀搅拌条件下,往铝盐与锰盐混合溶液中缓慢加入适量氧化剂溶液,继续搅拌15min-2h以保证充分反应,之后加入适量碱液调节溶液pH值为6-8,然后加入适量分子筛到溶液中,先充分振荡,再静置陈化2-24h,最后将分子筛取出并经水洗和干燥过程制备而得。A method for preparing an aluminum-manganese composite oxide-modified molecular sieve, comprising preparing a mixed solution of aluminum salt and manganese salt, slowly adding an appropriate amount of oxidant solution to the mixed solution of aluminum salt and manganese salt under uniform stirring, and continuing to stir for 15min-2h In order to ensure full reaction, add an appropriate amount of lye to adjust the pH value of the solution to 6-8, then add an appropriate amount of molecular sieve into the solution, first fully shake, then stand and age for 2-24 hours, and finally remove the molecular sieve and wash and dry it Prepared.
所述的铝锰复合氧化物改性分子筛的制备方法,所述铝盐溶液包括硫酸铝、氯化铝、聚合硫酸铝、聚合氯化铝、明矾中的一种或其任意比混合物;所述的锰盐选自氯化锰、硫酸锰、硝酸锰中的一种或其任意比混合物。In the preparation method of the aluminum-manganese composite oxide modified molecular sieve, the aluminum salt solution includes one of aluminum sulfate, aluminum chloride, polyaluminum sulfate, polyaluminum chloride, alum, or a mixture thereof in any ratio; The manganese salt is selected from one of manganese chloride, manganese sulfate, manganese nitrate or any mixture thereof.
所述的铝锰复合氧化物改性分子筛的制备方法,所述的铝盐与锰盐满足铝锰摩尔比为1∶1至18∶1,加入氧化剂后的反应时间为15min至2h。In the preparation method of the molecular sieve modified by the aluminum-manganese composite oxide, the molar ratio of the aluminum salt and the manganese salt is 1:1 to 18:1, and the reaction time after adding the oxidant is 15 minutes to 2 hours.
所述的铝锰复合氧化物改性分子筛的制备方法,所用的碱液为氢氧化钠、氢氧化钾、碳酸钠、碳酸钾中的一种或其任意比的混合物。In the preparation method of the aluminum-manganese composite oxide modified molecular sieve, the lye used is one of sodium hydroxide, potassium hydroxide, sodium carbonate, potassium carbonate or a mixture thereof in any ratio.
所述的铝锰复合氧化物改性分子筛的制备方法,所述氧化剂溶液为高锰酸盐,氧化剂与所述锰盐的摩尔比为2∶3。In the preparation method of the aluminum-manganese composite oxide-modified molecular sieve, the oxidant solution is permanganate, and the molar ratio of the oxidant to the manganese salt is 2:3.
所述的铝锰复合氧化物改性分子筛的制备方法,所述氧化剂溶液为次氯酸盐、过氧化氢、液氯等中的一种,氧化剂溶液与锰盐的摩尔比为1∶1。In the preparation method of the aluminum-manganese composite oxide-modified molecular sieve, the oxidant solution is one of hypochlorite, hydrogen peroxide, liquid chlorine, etc., and the molar ratio of the oxidant solution to the manganese salt is 1:1.
所述的铝锰复合氧化物改性分子筛的制备方法,所述负载基体选自粒径范围0.2mm-2mm的分子筛,其种类为3A型、4A型、5A型、13X型和HY型中的一种或两种以上的任意组合。In the preparation method of the aluminum-manganese composite oxide modified molecular sieve, the supporting matrix is selected from molecular sieves with a particle size range of 0.2mm-2mm, and the types are 3A, 4A, 5A, 13X and HY. One or any combination of two or more.
所述的铝锰复合氧化物改性分子筛的制备方法,分子筛加入混合液后,振荡时间为0.5-12h,且所述陈化步骤的温度为室温、陈化时间为2-24小时。In the preparation method of the molecular sieve modified by the aluminum-manganese composite oxide, after the molecular sieve is added to the mixed liquid, the shaking time is 0.5-12 hours, and the temperature of the aging step is room temperature, and the aging time is 2-24 hours.
所述的铝锰复合氧化物改性分子筛的制备方法,所述的干燥步骤是在50-75℃条件下干燥6-24小时,之后再升温至90-180℃干燥3-12小时。In the preparation method of the aluminum-manganese composite oxide-modified molecular sieve, the drying step is to dry at 50-75°C for 6-24 hours, and then raise the temperature to 90-180°C for 3-12 hours.
本发明特点:Features of the present invention:
铝锰复合氧化物改性分子筛吸附剂制备过程简单、成本低廉。The preparation process of the aluminum-manganese composite oxide modified molecular sieve adsorbent is simple and low in cost.
铝锰复合氧化物改性分子筛吸附剂可对三价砷As(III)和五价砷As(V)等污染物均表现出良好的去除效果。Al-Mn composite oxide modified molecular sieve adsorbent can show good removal effect on trivalent arsenic As(III) and pentavalent arsenic As(V) and other pollutants.
所制备的铝锰复合氧化物改性分子筛吸附剂具有吸附速度快、容量大,具有优异的水质净化效能。The prepared aluminum-manganese composite oxide modified molecular sieve adsorbent has fast adsorption speed, large capacity and excellent water purification performance.
具体实施方式Detailed ways
以下结合具体实施例,对本发明进行详细说明。The present invention will be described in detail below in conjunction with specific embodiments.
实施例1 铝锰复合氧化物/分子筛吸附剂的制备:配置200ml 0.25mol/L的氯化铝和0.15mol/L的氯化锰混合溶液。快速搅拌条件下往铝锰盐混合溶液中加入200ml0.1mol/L高锰酸钾溶液,继续搅拌15min,之后用氢氧化钠溶液(0.01M-5M)调节溶液pH为6-8;然后将200g粒径为0.2mm-0.5mm的3A型分子筛加入到混合液中,振荡30分钟,然后静置、室温陈化2小时。经陈化,撇去上清液,再加入少量稀碱液或稀酸液中和至中性,然后加入200ml去离子水,搅拌、洗涤10分钟,用过滤方法进行固液分离,固体吸附剂继续加去离子水洗涤3-4次,分离出吸附剂后,将其置于烘箱中于50℃下烘24小时,升温至90℃保持12小时,即得铝锰复合氧化物/分子筛吸附剂试样1。Example 1 Preparation of aluminum-manganese composite oxide/molecular sieve adsorbent: Prepare 200ml of a mixed solution of 0.25mol/L aluminum chloride and 0.15mol/L manganese chloride. Add 200ml0.1mol/L potassium permanganate solution to the aluminum-manganese salt mixed solution under rapid stirring, continue stirring for 15min, and then adjust the pH of the solution to 6-8 with sodium hydroxide solution (0.01M-5M); then add 200g 3A molecular sieves with a particle size of 0.2mm-0.5mm were added to the mixture, shaken for 30 minutes, then left to stand and aged at room temperature for 2 hours. After aging, skim off the supernatant, then add a small amount of dilute lye or dilute acid to neutralize, then add 200ml of deionized water, stir and wash for 10 minutes, and separate solid and liquid by filtration. Continue to add deionized water to wash for 3-4 times. After the adsorbent is separated, put it in an oven and bake it at 50°C for 24 hours, then raise the temperature to 90°C and keep it for 12 hours to obtain the aluminum-manganese composite oxide/molecular sieve adsorbent Sample 1.
实施例2 铝锰复合氧化物/分子筛吸附剂的制备:配置200ml 0.25mol/L的硫酸铝和0.15mol/L的硫酸锰混合溶液。快速搅拌条件下往铝锰盐混合溶液中加入200ml0.1mol/L高锰酸钾溶液,继续搅拌30min,之后用氢氧化钾溶液(0.01M-5M)调节溶液pH为6-8;然后将200g粒径为0.5mm-0.8mm的5A型分子筛加入到混合液中,振荡1h,然后静置、室温陈化6小时。经陈化,撇去上清液,再加入少量稀碱液或稀酸液中和至中性,然后加入200ml去离子水,搅拌、洗涤10分钟,用过滤方法进行固液分离,固体吸附剂继续加去离子水洗涤3-4次,分离出吸附剂后,将其置于烘箱中于55℃下烘18小时,升温至100℃保持10小时,即得铝锰复合氧化物/分子筛吸附剂试样2。Example 2 Preparation of aluminum-manganese composite oxide/molecular sieve adsorbent: Prepare 200ml of a mixed solution of 0.25mol/L aluminum sulfate and 0.15mol/L manganese sulfate. Add 200ml0.1mol/L potassium permanganate solution to the aluminum-manganese salt mixed solution under rapid stirring, continue stirring for 30min, and then adjust the pH of the solution to 6-8 with potassium hydroxide solution (0.01M-5M); then add 200g 5A molecular sieves with a particle size of 0.5mm-0.8mm were added to the mixture, shaken for 1 hour, then left to stand and aged at room temperature for 6 hours. After aging, skim off the supernatant, then add a small amount of dilute lye or dilute acid to neutralize, then add 200ml of deionized water, stir and wash for 10 minutes, and separate solid and liquid by filtration. Continue to add deionized water to wash for 3-4 times. After the adsorbent is separated, put it in an oven and bake it at 55°C for 18 hours, then raise the temperature to 100°C and keep it for 10 hours to obtain the aluminum-manganese composite oxide/molecular sieve adsorbent Sample 2.
实施例3 铝锰复合氧化物/分子筛吸附剂的制备:配置200ml 0.45mol/L的明矾和0.15mol/L的硝酸锰混合溶液。在快速搅拌条件下,往铝锰盐混合溶液中加入适量过氧化氢溶液,使氧化剂与锰盐的摩尔比为1∶1,继续搅拌1h,并用碳酸钠溶液(0.01M-5M)调节溶液浓度为6-8;然后将200g粒径为0.8mm-1.0mm的13X型分子筛加入到混合液中,振荡3h,然后静置、室温陈化10小时。经陈化,撇去上清液,再加入少量稀碱液中和至中性,然后加入200ml去离子水,搅拌、洗涤10分钟,用过滤方法进行固液分离,固体吸附剂继续加去离子水洗涤3-4次,分离出吸附剂后,将其置于烘箱中于60℃下烘12小时,升温至110℃保持8小时,即得铝锰复合氧化物/分子筛吸附剂试样3。Example 3 Preparation of aluminum-manganese composite oxide/molecular sieve adsorbent: Prepare 200ml of a mixed solution of 0.45mol/L alum and 0.15mol/L manganese nitrate. Under rapid stirring conditions, add an appropriate amount of hydrogen peroxide solution to the mixed solution of aluminum-manganese salt, so that the molar ratio of oxidant and manganese salt is 1:1, continue stirring for 1 hour, and adjust the concentration of the solution with sodium carbonate solution (0.01M-5M) 6-8; then 200g of 13X molecular sieves with a particle size of 0.8mm-1.0mm were added to the mixture, shaken for 3 hours, then left to stand and aged at room temperature for 10 hours. After aging, skim the supernatant, then add a small amount of dilute lye to neutralize to neutral, then add 200ml deionized water, stir and wash for 10 minutes, separate solid-liquid by filtration, and continue to add deionized solid adsorbent After washing with water for 3-4 times and separating the adsorbent, put it in an oven and bake it at 60°C for 12 hours, then raise the temperature to 110°C and keep it for 8 hours to obtain Al-Mn composite oxide/molecular sieve adsorbent sample 3.
实施例4 铝锰复合氧化物/分子筛吸附剂的制备:配置200ml的聚合硫酸铝和硫酸锰混合溶液,使铝锰的摩尔比为6∶1。在快速搅拌条件下,往铝锰盐混合溶液中加入适量次氯酸钠溶液,使氧化剂与锰盐的摩尔比为1∶1,继续搅拌1.5h,并用碳酸钾溶液(0.01M-5M)调节溶液浓度为6-8;然后将200g粒径为1.0mm-1.5mm的5A型分子筛加入到混合液中,振荡6h,然后静置、室温陈化16小时。经陈化,撇去上清液,再加入少量稀碱液中和至中性,然后加入200ml去离子水,搅拌、洗涤10分钟,用过滤方法进行固液分离,固体吸附剂继续加去离子水洗涤3-4次,分离出吸附剂后,将其置于烘箱中于65℃下烘9小时,升温至150℃保持6小时,即得铝锰复合氧化物/分子筛吸附剂试样4。Example 4 Preparation of aluminum-manganese composite oxide/molecular sieve adsorbent: Prepare 200ml of mixed solution of polyaluminum sulfate and manganese sulfate, so that the molar ratio of aluminum to manganese is 6:1. Under rapid stirring conditions, add an appropriate amount of sodium hypochlorite solution to the mixed solution of aluminum-manganese salt, so that the molar ratio of oxidant and manganese salt is 1:1, continue stirring for 1.5h, and adjust the solution concentration with potassium carbonate solution (0.01M-5M). 6-8; Then add 200g of 5A molecular sieves with a particle size of 1.0mm-1.5mm into the mixture, shake for 6h, then stand still and age at room temperature for 16 hours. After aging, skim the supernatant, then add a small amount of dilute lye to neutralize to neutral, then add 200ml deionized water, stir and wash for 10 minutes, separate solid-liquid by filtration, and continue to add deionized solid adsorbent After washing with water for 3-4 times and separating the adsorbent, put it in an oven and bake it at 65°C for 9 hours, then raise the temperature to 150°C and keep it for 6 hours to obtain Al-Mn composite oxide/molecular sieve adsorbent sample 4.
实施例5 铝锰复合氧化物/分子筛吸附剂的制备:配置200ml的聚合氯化铝和氯化锰混合溶液,使铝锰盐的摩尔比为9∶1。在快速搅拌条件下,往铝锰盐混合溶液中加入适量液氯溶液,使氧化剂与锰盐的摩尔比为1∶1,继续搅拌2h,并用氢氧化钠溶液(0.01M-5M)调节溶液浓度为6-8;然后将200g粒径为1.5mm-1.7mm的13X型分子筛加入到混合液中,振荡12h,然后静置、室温陈化24小时。经陈化,撇去上清液,再加入少量稀碱液中和至中性,然后加入200ml去离子水,搅拌、洗涤10分钟,用过滤方法进行固液分离,固体吸附剂继续加去离子水洗涤3-4次,分离出吸附剂后,将其置于烘箱中于75℃下烘6小时,升温至180℃保持3小时,即得铝锰复合氧化物/分子筛吸附剂试样5。Example 5 Preparation of aluminum-manganese composite oxide/molecular sieve adsorbent: Prepare 200ml of mixed solution of polyaluminum chloride and manganese chloride so that the molar ratio of aluminum-manganese salt is 9:1. Under the condition of rapid stirring, add an appropriate amount of liquid chlorine solution to the mixed solution of aluminum-manganese salt, so that the molar ratio of oxidant and manganese salt is 1:1, continue to stir for 2 hours, and adjust the concentration of the solution with sodium hydroxide solution (0.01M-5M) 6-8; then 200g of 13X molecular sieves with a particle size of 1.5mm-1.7mm were added to the mixture, shaken for 12h, then left to stand and aged at room temperature for 24 hours. After aging, skim the supernatant, then add a small amount of dilute lye to neutralize to neutral, then add 200ml deionized water, stir and wash for 10 minutes, separate solid-liquid by filtration, and continue to add deionized solid adsorbent After washing with water for 3-4 times and separating the adsorbent, put it in an oven and bake it at 75°C for 6 hours, then raise the temperature to 180°C and keep it for 3 hours to obtain Al-Mn composite oxide/molecular sieve adsorbent sample 5.
实施例6 铝锰复合氧化物/分子筛吸附剂的制备:配置200ml的氯化铝和氯化锰混合溶液,使铝锰盐的摩尔比为18∶1。在快速搅拌条件下,往铝锰盐混合溶液中加入适量次氯酸钾溶液,使氧化剂与锰盐的摩尔比为1∶1,继续搅拌2h,并用氢氧化钾溶液(0.01M-5M)调节溶液浓度为6-8;然后将200g粒径为1.7mm-2.0mm的HY型分子筛加入到混合液中,振荡12h,然后静置、室温陈化24小时。经陈化,撇去上清液,再加入少量稀碱液中和至中性,然后加入200ml去离子水,搅拌、洗涤10分钟,用过滤方法进行固液分离,固体吸附剂继续加去离子水洗涤3-4次,分离出吸附剂后,将其置于烘箱中于75℃下烘6小时,升温至180℃保持3小时,即得铝锰复合氧化物/分子筛吸附剂试样5。Example 6 Preparation of aluminum-manganese composite oxide/molecular sieve adsorbent: Prepare 200ml of mixed solution of aluminum chloride and manganese chloride so that the molar ratio of aluminum-manganese salt is 18:1. Under rapid stirring conditions, add an appropriate amount of potassium hypochlorite solution to the mixed solution of aluminum-manganese salt, so that the molar ratio of oxidant and manganese salt is 1:1, continue stirring for 2 hours, and adjust the solution concentration with potassium hydroxide solution (0.01M-5M) 6-8; then add 200g of HY-type molecular sieves with a particle size of 1.7mm-2.0mm into the mixture, shake it for 12 hours, then let it stand and age at room temperature for 24 hours. After aging, skim the supernatant, then add a small amount of dilute lye to neutralize to neutral, then add 200ml deionized water, stir and wash for 10 minutes, separate solid-liquid by filtration, and continue to add deionized solid adsorbent After washing with water for 3-4 times and separating the adsorbent, put it in an oven and bake it at 75°C for 6 hours, then raise the temperature to 180°C and keep it for 3 hours to obtain Al-Mn composite oxide/molecular sieve adsorbent sample 5.
实施例7 铝锰复合氧化物/分子筛吸附剂在含砷废水处理中的应用:本发明所用的反应器为一玻璃填充柱,其中填有制备的铝锰氧化物/分子筛吸附剂颗粒,柱高约0.8m,直径5cm,填充体积750cm3。某含砷废水,三价砷As(III)浓度100μg/L,pH=7.2。从填充柱下方进水,上端出水,进水流量50ml/min,定期测定出水砷浓度。流经约5400倍填充体积后,出水中砷浓度才高于10μg/L。Example 7 Application of aluminum-manganese composite oxide/molecular sieve adsorbent in the treatment of arsenic-containing wastewater: the reactor used in the present invention is a glass packed column filled with the prepared aluminum-manganese oxide/molecular sieve adsorbent particles, the column height About 0.8m, diameter 5cm, filling volume 750cm 3 . In a certain arsenic-containing wastewater, the concentration of trivalent arsenic As(III) is 100 μg/L, and pH=7.2. Water is fed from the bottom of the packed column, and water is discharged from the upper end. The flow rate of the incoming water is 50ml/min, and the concentration of arsenic in the discharged water is regularly measured. After about 5400 times the filling volume, the arsenic concentration in the effluent was higher than 10 μg/L.
实施例8 铝锰复合氧化物/分子筛吸附剂的原位再生:当填充柱出水中砷浓度高于水质要求时,停止进水,放空柱中水后,从填充柱的下方缓慢泵入加有碱液100ml浓度为30%的次氯酸钠溶液,然后从填充柱上方缓慢加入100ml 0.5mol/L的氢氧化钠溶液,流速均为1ml/min。加毕,静止陈化4小时,然后放出水相,用去离子水冲洗填充柱,直至出水中溶解性铝锰离子的浓度低于水质要求。Example 8 In-situ regeneration of aluminum-manganese composite oxide/molecular sieve adsorbent: When the concentration of arsenic in the effluent water of the packed column is higher than the water quality requirement, stop the water inflow, and after emptying the water in the column, slowly pump in the arsenic from the bottom of the packed column. Alkaline 100ml concentration is 30% sodium hypochlorite solution, then slowly add 100ml 0.5mol/L sodium hydroxide solution from the top of the packed column, the flow rate is 1ml/min. After the addition is completed, it is statically aged for 4 hours, and then the water phase is released, and the packed column is washed with deionized water until the concentration of soluble aluminum-manganese ions in the effluent is lower than the water quality requirement.
应当理解的是,对本领域普通技术人员来说,可以根据上述说明加以改进或变换,而所有这些改进和变换都应属于本发明所附权利要求的保护范围。It should be understood that those skilled in the art can make improvements or changes based on the above description, and all these improvements and changes should belong to the protection scope of the appended claims of the present invention.
Claims (9)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN2010105432592A CN102008939B (en) | 2010-11-15 | 2010-11-15 | Method for preparing aluminum-manganese composite oxide modified molecular sieve |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN2010105432592A CN102008939B (en) | 2010-11-15 | 2010-11-15 | Method for preparing aluminum-manganese composite oxide modified molecular sieve |
Publications (2)
Publication Number | Publication Date |
---|---|
CN102008939A true CN102008939A (en) | 2011-04-13 |
CN102008939B CN102008939B (en) | 2012-07-25 |
Family
ID=43839382
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN2010105432592A Expired - Fee Related CN102008939B (en) | 2010-11-15 | 2010-11-15 | Method for preparing aluminum-manganese composite oxide modified molecular sieve |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN102008939B (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102580670A (en) * | 2012-02-20 | 2012-07-18 | 中国地质大学(武汉) | Arsenic removal material of nanometer ferrimanganic binary oxide loaded by zeolite and preparation method of arsenic removal material |
CN109592720A (en) * | 2018-11-23 | 2019-04-09 | 湖南中伟新能源科技有限公司 | Ternary precursor solution purification method |
Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US6042731A (en) * | 1997-01-31 | 2000-03-28 | The University Of South Florida | Method of removing arsenic species from an aqueous medium using modified zeolite minerals |
US20030017936A1 (en) * | 2000-11-01 | 2003-01-23 | Kyung-Byung Yoon | Zeolite-substrate composite comprising a patterned zeolite layer on a substrate and preparation thereof |
CN1632061A (en) * | 2004-12-01 | 2005-06-29 | 中国石油天然气股份有限公司 | Selective cracking catalyst for producing low-carbon olefin |
CN101579638A (en) * | 2009-06-29 | 2009-11-18 | 清华大学 | Catalyst for preparing ethylene by ethanol dehydration and preparation method thereof |
CN101628242A (en) * | 2009-08-10 | 2010-01-20 | 大唐国际化工技术研究院有限公司 | Molecular sieve catalyst for preparing low-carbon olefin and preparation method thereof |
-
2010
- 2010-11-15 CN CN2010105432592A patent/CN102008939B/en not_active Expired - Fee Related
Patent Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US6042731A (en) * | 1997-01-31 | 2000-03-28 | The University Of South Florida | Method of removing arsenic species from an aqueous medium using modified zeolite minerals |
US20030017936A1 (en) * | 2000-11-01 | 2003-01-23 | Kyung-Byung Yoon | Zeolite-substrate composite comprising a patterned zeolite layer on a substrate and preparation thereof |
CN1632061A (en) * | 2004-12-01 | 2005-06-29 | 中国石油天然气股份有限公司 | Selective cracking catalyst for producing low-carbon olefin |
CN101579638A (en) * | 2009-06-29 | 2009-11-18 | 清华大学 | Catalyst for preparing ethylene by ethanol dehydration and preparation method thereof |
CN101628242A (en) * | 2009-08-10 | 2010-01-20 | 大唐国际化工技术研究院有限公司 | Molecular sieve catalyst for preparing low-carbon olefin and preparation method thereof |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102580670A (en) * | 2012-02-20 | 2012-07-18 | 中国地质大学(武汉) | Arsenic removal material of nanometer ferrimanganic binary oxide loaded by zeolite and preparation method of arsenic removal material |
CN102580670B (en) * | 2012-02-20 | 2014-03-26 | 中国地质大学(武汉) | Arsenic removal material of nanometer ferrimanganic binary oxide loaded by zeolite and preparation method of arsenic removal material |
CN109592720A (en) * | 2018-11-23 | 2019-04-09 | 湖南中伟新能源科技有限公司 | Ternary precursor solution purification method |
Also Published As
Publication number | Publication date |
---|---|
CN102008939B (en) | 2012-07-25 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN100435931C (en) | Compound metal oxide de-fluorine sorbent | |
CN102527347A (en) | Magnetic chitosan/cationic surface active agent modified zeolite adsorbent and preparation method and application thereof | |
CN101024160A (en) | Preparation of iron-managanese compounded oxide/diatomite adsorbant, its using and regenerating method | |
CN103752268A (en) | Preparation method of filter core for adsorbing heavy metal, arsenic and fluorine in drinking water and application thereof | |
CN102001722B (en) | Method for removing phosphate from water by using zirconia-modified mesoporous silicon material | |
CN112169748B (en) | A kind of adsorbent and its preparation method and application | |
CN104492381A (en) | Heterogeneous TiO2/Co metal organic framework material and its preparation method and application | |
CN106902744A (en) | The method that one kind prepares MIL 100 (Fe) at room temperature | |
CN106824100A (en) | A kind of zinc MOF poromerics of efficient capture iodine and preparation method and application | |
CN107469760A (en) | A kind of nanometer CaTiO3Powder adsorbent and its preparation method and application | |
CN108940235A (en) | The in-situ precipitate preparation method and application of geo-polymer defluorinating agent | |
CN106824046A (en) | A kind of copper cerium codope magnetic composite and its methods for making and using same | |
CN109107524B (en) | A kind of red mud adsorbent and its preparation method and application | |
CN106215846B (en) | A kind of magnalium silicon composite adsorbing material and its preparation method and application | |
CN101966444B (en) | Preparation method of dephosphorisation absorptive material and application thereof | |
CN102008939B (en) | Method for preparing aluminum-manganese composite oxide modified molecular sieve | |
CN112076752A (en) | A kind of MOF-74 derived magnetic composite catalyst and its preparation method and application | |
CN102886239A (en) | Method for preparing iron-titanium oxide serving as defluorination adsorbent | |
CN114262034B (en) | Method for separating rubidium from salt lake brine by using polyvinyl alcohol/chitosan/graphene/nickel copper hexacyanide complex | |
CN112121772A (en) | Defluorination wood film filtering device | |
CN105251531B (en) | A kind of preparation of ultralow mercury catalyst with long service life and its recovery method | |
CN109999759A (en) | A kind of processing Pb In Exhausted Water ion modification chitosan absorbent and preparation method thereof | |
CN102276009A (en) | Method for removing fluorin from water by utilizing cerium-oxide-loaded attapulgite | |
CN108187607A (en) | A kind of ethylene-ethane separation adsorption separating agent and its preparation method and application | |
CN107597115A (en) | It is a kind of can high-efficient purification high concentration arsenic hydride catalyst and preparation method thereof |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
C06 | Publication | ||
PB01 | Publication | ||
C10 | Entry into substantive examination | ||
SE01 | Entry into force of request for substantive examination | ||
C14 | Grant of patent or utility model | ||
GR01 | Patent grant | ||
C17 | Cessation of patent right | ||
CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20120725 Termination date: 20121115 |