CN104162404B - Preparation method of adsorbent of rare earth doped hydrated manganese oxide - Google Patents
Preparation method of adsorbent of rare earth doped hydrated manganese oxide Download PDFInfo
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- AMWRITDGCCNYAT-UHFFFAOYSA-L hydroxy(oxo)manganese;manganese Chemical compound [Mn].O[Mn]=O.O[Mn]=O AMWRITDGCCNYAT-UHFFFAOYSA-L 0.000 title claims abstract description 56
- 239000003463 adsorbent Substances 0.000 title claims abstract description 28
- 238000002360 preparation method Methods 0.000 title claims description 21
- 229910052761 rare earth metal Inorganic materials 0.000 title abstract description 10
- 150000002910 rare earth metals Chemical class 0.000 title abstract description 10
- 239000000243 solution Substances 0.000 claims abstract description 63
- 239000011259 mixed solution Substances 0.000 claims abstract description 48
- NUJOXMJBOLGQSY-UHFFFAOYSA-N manganese dioxide Chemical compound O=[Mn]=O NUJOXMJBOLGQSY-UHFFFAOYSA-N 0.000 claims abstract description 36
- 239000013078 crystal Substances 0.000 claims abstract description 19
- FAPWRFPIFSIZLT-UHFFFAOYSA-M Sodium chloride Chemical compound [Na+].[Cl-] FAPWRFPIFSIZLT-UHFFFAOYSA-M 0.000 claims abstract description 17
- 238000000034 method Methods 0.000 claims abstract description 17
- 239000002245 particle Substances 0.000 claims abstract description 13
- 239000012065 filter cake Substances 0.000 claims abstract description 9
- 239000002244 precipitate Substances 0.000 claims abstract description 4
- 238000006243 chemical reaction Methods 0.000 claims description 10
- 238000003756 stirring Methods 0.000 claims description 8
- 230000035484 reaction time Effects 0.000 claims description 3
- 238000001556 precipitation Methods 0.000 claims description 2
- 239000002594 sorbent Substances 0.000 claims 7
- 239000002689 soil Substances 0.000 claims 3
- 238000003825 pressing Methods 0.000 claims 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims 2
- 238000002156 mixing Methods 0.000 claims 1
- 238000001179 sorption measurement Methods 0.000 abstract description 18
- 238000004065 wastewater treatment Methods 0.000 abstract description 10
- 239000011780 sodium chloride Substances 0.000 abstract description 7
- 230000003321 amplification Effects 0.000 abstract description 6
- 238000003199 nucleic acid amplification method Methods 0.000 abstract description 6
- 238000011085 pressure filtration Methods 0.000 abstract description 5
- 239000013049 sediment Substances 0.000 abstract description 5
- 230000036632 reaction speed Effects 0.000 abstract description 4
- PWHULOQIROXLJO-UHFFFAOYSA-N Manganese Chemical compound [Mn] PWHULOQIROXLJO-UHFFFAOYSA-N 0.000 abstract 1
- 229910052748 manganese Inorganic materials 0.000 abstract 1
- 239000011572 manganese Substances 0.000 abstract 1
- 229910001385 heavy metal Inorganic materials 0.000 description 11
- 239000002351 wastewater Substances 0.000 description 11
- 229910044991 metal oxide Inorganic materials 0.000 description 7
- 229910052716 thallium Inorganic materials 0.000 description 6
- 229910052793 cadmium Inorganic materials 0.000 description 3
- BDOSMKKIYDKNTQ-UHFFFAOYSA-N cadmium atom Chemical compound [Cd] BDOSMKKIYDKNTQ-UHFFFAOYSA-N 0.000 description 3
- 229910052753 mercury Inorganic materials 0.000 description 3
- 239000000203 mixture Substances 0.000 description 3
- BKVIYDNLLOSFOA-UHFFFAOYSA-N thallium Chemical compound [Tl] BKVIYDNLLOSFOA-UHFFFAOYSA-N 0.000 description 3
- UQSXHKLRYXJYBZ-UHFFFAOYSA-N Iron oxide Chemical compound [Fe]=O UQSXHKLRYXJYBZ-UHFFFAOYSA-N 0.000 description 2
- VYLVYHXQOHJDJL-UHFFFAOYSA-K cerium trichloride Chemical compound Cl[Ce](Cl)Cl VYLVYHXQOHJDJL-UHFFFAOYSA-K 0.000 description 2
- 150000004706 metal oxides Chemical class 0.000 description 2
- 208000005156 Dehydration Diseases 0.000 description 1
- 125000002091 cationic group Chemical group 0.000 description 1
- 150000001768 cations Chemical class 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 238000000975 co-precipitation Methods 0.000 description 1
- 230000002860 competitive effect Effects 0.000 description 1
- 230000018044 dehydration Effects 0.000 description 1
- 238000006297 dehydration reaction Methods 0.000 description 1
- 238000003795 desorption Methods 0.000 description 1
- 230000018109 developmental process Effects 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 239000003344 environmental pollutant Substances 0.000 description 1
- 125000002887 hydroxy group Chemical group [H]O* 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- JJIJKNKBEFFVIK-UHFFFAOYSA-N manganese(2+);oxygen(2-);hydrate Chemical compound O.[O-2].[Mn+2] JJIJKNKBEFFVIK-UHFFFAOYSA-N 0.000 description 1
- 230000007246 mechanism Effects 0.000 description 1
- 239000002105 nanoparticle Substances 0.000 description 1
- 231100000719 pollutant Toxicity 0.000 description 1
- 239000012286 potassium permanganate Substances 0.000 description 1
- 238000006479 redox reaction Methods 0.000 description 1
- 238000006722 reduction reaction Methods 0.000 description 1
- 230000008929 regeneration Effects 0.000 description 1
- 238000011069 regeneration method Methods 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
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Abstract
本发明公开了一种稀土掺杂水合氧化锰的吸附剂制备方法,首先采用摩尔浓度2%~5%的MnSO4·H2O溶液与2%~10%的NaCl溶液配制混合液Ⅰ,向混合液Ⅰ中加入0.1%~0.5%的KMnO4溶液,制得水合二氧化锰晶种混合液;对水合二氧化锰晶种混合液进行稀土掺杂晶粒放大处理;对稀土掺杂水合氧化锰混合液进行沉淀物粒径分级处理,取粒径大于10μm的沉淀物进行压滤处理,得到的吸附剂滤饼;将吸附剂滤饼在50℃~75℃条件下干燥1.5h~3h,至表面无明显水分,得到最终的吸附剂。该吸附剂吸附反应速度快、吸附容量高,从而减少其在废水处理过程中的投加量,降低了废水处理的运行成本。
The invention discloses a method for preparing an adsorbent of rare earth-doped hydrated manganese oxide. Firstly, a mixed solution I is prepared by using a MnSO 4 ·H 2 O solution with a molar concentration of 2% to 5% and a NaCl solution of 2% to 10%. Add 0.1% to 0.5% KMnO 4 solution to the mixed solution I to prepare the hydrated manganese dioxide seed crystal mixed solution; perform rare earth doping crystal grain amplification treatment on the hydrated manganese dioxide seed mixed solution; hydrate and oxidize the rare earth doped The manganese mixed solution is subjected to sediment particle size classification treatment, and the precipitate with a particle size greater than 10 μm is subjected to pressure filtration treatment to obtain an adsorbent filter cake; the adsorbent filter cake is dried at 50°C to 75°C for 1.5h to 3h, Until the surface has no obvious moisture, the final adsorbent is obtained. The adsorbent has fast adsorption reaction speed and high adsorption capacity, thereby reducing its dosage in the waste water treatment process and reducing the operating cost of the waste water treatment.
Description
技术领域technical field
本发明涉及废水处理技术领域,尤其涉及一种稀土掺杂水合氧化锰的吸附剂制备方法。The invention relates to the technical field of wastewater treatment, in particular to a method for preparing an adsorbent of rare earth-doped hydrated manganese oxide.
背景技术Background technique
目前,传统纳米金属氧化物(如水合氧化锰、水合氧化铁等)等对废水中铊、镉等阳离子型重金属具有较高的吸附容量。纳米金属氧化物在溶液体系中的等温吸附容量、多离子竞争吸附关系、解吸再生性能等内容研究较多,然而纳米金属氧化物却在废水处理工程应用较少,这主要是由于存在如下几点技术难点:首先,纳米金属氧化物的粒径小,纳米级的氧化物颗粒在吸附重金属后,难以从废水中沉淀分离,从而导致处理后的废水中总重金属浓度并未显著降低。其次,纳米金属氧化物的吸附选择性不强,难以去除废水中微量的重金属。当废水中Ca2+、Pb2+等阳离子浓度远高于需要去除的目标重金属污染物(如Tl、Hg等)浓度时,吸附剂的表面羟基点位被浓度更高的Ca2+、Pb2+占据,使得处理出水中残留的微量重金属仍难以达到深度处理的出水要求。At present, traditional nano-metal oxides (such as hydrated manganese oxide, hydrated iron oxide, etc.) have high adsorption capacity for cationic heavy metals such as thallium and cadmium in wastewater. There are many studies on the isothermal adsorption capacity, multi-ion competitive adsorption relationship, and desorption regeneration performance of nano-metal oxides in solution systems. However, nano-metal oxides are rarely used in wastewater treatment projects. This is mainly due to the following points Technical difficulties: First, the particle size of nano-sized metal oxides is small, and it is difficult for nano-scale oxide particles to precipitate and separate from wastewater after adsorbing heavy metals, resulting in no significant reduction in the total heavy metal concentration in treated wastewater. Secondly, the adsorption selectivity of nano-metal oxides is not strong, and it is difficult to remove trace heavy metals in wastewater. When the concentration of Ca 2+ , Pb 2+ and other cations in the wastewater is much higher than the concentration of the target heavy metal pollutants (such as Tl, Hg, etc.) 2+ occupation, making it difficult to meet the effluent requirements of advanced treatment for trace heavy metals remaining in the treated effluent.
因此,开发一种对废水中微量重金属(如Tl、Hg等)具有高度选择性吸附、吸附容量高、且易于沉淀分离的金属氧化物吸附剂具有重要的推广应用前景与经济社会价值。Therefore, the development of a metal oxide adsorbent with highly selective adsorption for trace heavy metals (such as Tl, Hg, etc.) in wastewater, high adsorption capacity, and easy precipitation and separation has important application prospects and economic and social value.
发明内容Contents of the invention
本发明的目的是提供一种稀土掺杂水合氧化锰的吸附剂制备方法,采用该制备方法制得的吸附剂吸附反应速度快、吸附容量高,从而减少其在废水处理过程中的投加量,降低了废水处理的运行成本。The purpose of this invention is to provide a kind of adsorbent preparation method of rare earth doped hydrated manganese oxide, the adsorbent prepared by the preparation method has fast adsorption reaction speed and high adsorption capacity, thereby reducing its dosage in the wastewater treatment process , reducing the operating cost of wastewater treatment.
一种稀土掺杂水合氧化锰的吸附剂制备方法,所述制备方法包括:A method for preparing an adsorbent of rare earth-doped hydrated manganese oxide, the preparation method comprising:
采用摩尔浓度2%~5%的MnSO4·H2O溶液与2%~10%的NaCl溶液配制混合液Ⅰ,向所述混合液Ⅰ中加入0.1%~0.5%的KMnO4溶液,在设定的反应条件下制得水合二氧化锰晶种混合液;Mixed solution I was prepared by using MnSO 4 ·H 2 O solution with a molar concentration of 2% to 5% and NaCl solution with 2% to 10%, and added 0.1% to 0.5% KMnO 4 solution to the mixed solution I. Prepare the hydrated manganese dioxide seed crystal mixed solution under certain reaction conditions;
对所述水合二氧化锰晶种混合液进行稀土掺杂晶粒放大处理,具体包括:采用0.2%~1%的CeCl3溶液与2%~5%的MnSO4·H2O溶液,按照一定的体积比配制成混合液Ⅱ,将所述混合液Ⅱ与所述水合二氧化锰晶种混合液按照一定的体积比混合,配制成混合液Ⅲ,再向所述混合液Ⅲ中加入1%~3%KMnO4溶液,在20~40℃条件下,将混合溶液搅拌反应1.5~3h,得到稀土掺杂水合氧化锰混合液;The hydrated manganese dioxide seed mixture solution is subjected to rare earth doping crystal grain amplification treatment, which specifically includes: using 0.2% to 1% CeCl 3 solution and 2% to 5% MnSO 4 ·H 2 O solution, according to a certain The volume ratio of the mixed solution II is prepared into the mixed solution II, and the mixed solution II is mixed with the hydrated manganese dioxide seed crystal mixed solution according to a certain volume ratio to prepare the mixed solution III, and then 1% of the mixed solution is added to the mixed solution III ~3% KMnO 4 solution, under the condition of 20~40°C, stirring and reacting the mixed solution for 1.5~3 hours to obtain the rare earth doped hydrated manganese oxide mixed solution;
对所述稀土掺杂水合氧化锰混合液进行沉淀物粒径分级处理,取粒径大于10μm的沉淀物进行压滤处理,收集压滤处理后得到的吸附剂滤饼;The rare earth-doped hydrated manganese oxide mixed solution is subjected to sediment particle size classification treatment, and the precipitate with a particle size greater than 10 μm is subjected to pressure filtration treatment, and the adsorbent filter cake obtained after pressure filtration treatment is collected;
将所述吸附剂滤饼在50℃~75℃条件下干燥1.5h~3h,至表面无明显水分,得到最终的稀土掺杂水合氧化锰的吸附剂。The filter cake of the adsorbent is dried at 50° C. to 75° C. for 1.5 h to 3 h until there is no obvious moisture on the surface to obtain the final rare earth-doped hydrated manganese oxide adsorbent.
在所述水合二氧化锰晶种混合液制备过程中:During the preparation process of the hydrated manganese dioxide seed mixed solution:
所述KMnO4溶液的摩尔浓度优选为0.4%;所述MnSO4·H2O溶液的摩尔浓度优选为3%;所述NaCl溶液的摩尔浓度优选7%。The molar concentration of the KMnO 4 solution is preferably 0.4%; the molar concentration of the MnSO 4 ·H 2 O solution is preferably 3%; the molar concentration of the NaCl solution is preferably 7%.
在所述水合二氧化锰晶种混合液制备过程中:During the preparation process of the hydrated manganese dioxide seed mixed solution:
所述MnSO4·H2O溶液与所述NaCl溶液的体积比为5:1~2:1之间,优选3:1;The volume ratio of the MnSO 4 ·H 2 O solution to the NaCl solution is between 5:1 and 2:1, preferably 3:1;
且所述混合液Ⅰ与KMnO4溶液的体积比为4:1~1:1之间,优选2:1。And the volume ratio of the mixed solution I to the KMnO 4 solution is between 4:1 and 1:1, preferably 2:1.
所述设定的反应条件为:温度介于90~100℃之间,搅拌反应时间介于1.5~3h之间,优选2h。The set reaction conditions are as follows: the temperature is between 90-100° C., and the stirring reaction time is between 1.5-3 hours, preferably 2 hours.
在进行稀土掺杂晶粒放大处理的过程中:In the process of rare earth doped grain amplification treatment:
所采用的MnSO4·H2O溶液的浓度优选为3%,所采用的CeCl3溶液的浓度优选0.7%,且所述MnSO4·H2O溶液与CeCl3溶液按照8:1~12:1的体积比配制成混合液Ⅱ。The concentration of the MnSO 4 ·H 2 O solution used is preferably 3%, the concentration of the CeCl 3 solution used is preferably 0.7%, and the MnSO 4 ·H 2 O solution and the CeCl 3 solution are in accordance with the ratio of 8:1 to 12: The volume ratio of 1 was prepared as the mixed liquid II.
在进行稀土掺杂晶粒放大处理的过程中:In the process of rare earth doped grain amplification treatment:
所述混合液Ⅱ与所述水合二氧化锰晶种混合液的体积比为3:1~5:1之间,优选为4:1;The volume ratio of the mixed solution II to the hydrated manganese dioxide seed mixed solution is between 3:1 and 5:1, preferably 4:1;
在所述混合液Ⅲ中所加入的KMnO4溶液的摩尔浓度优选为2%,且所述混合液Ⅲ与所述KMnO4溶液的体积比为3:1~1:1之间,优选为2:1。 The molar concentration of the KMnO solution added to the mixed solution III is preferably 2%, and the volume ratio of the mixed solution III to the KMnO solution is between 3 :1 and 1:1, preferably 2 :1.
在进行稀土掺杂晶粒放大处理的过程中:In the process of rare earth doped grain amplification treatment:
所述混合溶液搅拌反应的时间优选为2h。The time for stirring and reacting the mixed solution is preferably 2 hours.
由上述本发明提供的技术方案可以看出,采用该制备方法制得的吸附剂吸附具有反应速度快、吸附容量高的特点,能够减少废水处理过程中吸附剂的投加量,降低了废水处理的运行成本。It can be seen from the above technical solution provided by the present invention that the adsorption of the adsorbent prepared by the preparation method has the characteristics of fast reaction speed and high adsorption capacity, which can reduce the dosage of adsorbent in the wastewater treatment process and reduce the waste water treatment. operating costs.
附图说明Description of drawings
为了更清楚地说明本发明实施例的技术方案,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,对于本领域的普通技术人员来讲,在不付出创造性劳动的前提下,还可以根据这些附图获得其他附图。In order to more clearly illustrate the technical solutions of the embodiments of the present invention, the following will briefly introduce the accompanying drawings that need to be used in the description of the embodiments. Obviously, the accompanying drawings in the following description are only some embodiments of the present invention. For Those of ordinary skill in the art can also obtain other drawings based on these drawings on the premise of not paying creative work.
图1为本发明实施例所提供稀土掺杂水合氧化锰的吸附剂制备方法流程示意图。Fig. 1 is a schematic flow chart of the preparation method of the adsorbent of rare earth doped hydrated manganese oxide provided by the embodiment of the present invention.
具体实施方式detailed description
下面结合本发明实施例中的附图,对本发明实施例中的技术方案进行清楚、完整地描述,显然,所描述的实施例仅仅是本发明一部分实施例,而不是全部的实施例。基于本发明的实施例,本领域普通技术人员在没有做出创造性劳动前提下所获得的所有其他实施例,都属于本发明的保护范围。The technical solutions in the embodiments of the present invention will be clearly and completely described below in conjunction with the accompanying drawings in the embodiments of the present invention. Obviously, the described embodiments are only some of the embodiments of the present invention, not all of them. Based on the embodiments of the present invention, all other embodiments obtained by persons of ordinary skill in the art without making creative efforts belong to the protection scope of the present invention.
本发明实施例利用溶液体系中的氧化还原反应、共沉淀淀反应等多种物理化学反应机制,制备得到富含表面羟基活性交换点位的稀土掺杂水合氧化锰吸附剂,该吸附剂能够应用于废水中铊、镉、铅等重金属的深度吸附去除。下面将结合附图对本发明实施例作进一步地详细描述,如图1所示为本发明实施例所提供稀土掺杂水合氧化锰的吸附剂制备方法流程示意图,所述方法包括:The embodiment of the present invention utilizes various physical and chemical reaction mechanisms such as oxidation-reduction reaction and co-precipitation reaction in the solution system to prepare a rare earth-doped hydrated manganese oxide adsorbent rich in surface hydroxyl active exchange sites, which can be applied to It is used for the deep adsorption and removal of heavy metals such as thallium, cadmium, and lead in wastewater. The embodiments of the present invention will be further described in detail below in conjunction with the accompanying drawings. Figure 1 is a schematic flow chart of the preparation method for the adsorbent of rare earth-doped hydrated manganese oxide provided by the embodiments of the present invention. The method includes:
步骤11:采用摩尔浓度为2%~5%的MnSO4·H2O溶液与2%~10%的NaCl溶液配制混合液Ⅰ,向所述混合液Ⅰ中加入0.1%~0.5%的KMnO4溶液,在设定的反应条件下制得水合二氧化锰晶种混合液;Step 11: Prepare a mixed solution I by using a MnSO 4 ·H 2 O solution with a molar concentration of 2% to 5% and a 2% to 10% NaCl solution, and add 0.1% to 0.5% KMnO 4 to the mixed solution I Solution, the hydrated manganese dioxide seed crystal mixed solution is obtained under the set reaction conditions;
在该步骤中,制备水合氧化锰晶种混合溶液的配方可以为:0.1%~0.5%摩尔浓度的KMnO4溶液,浓度优选0.4%;2%~5%摩尔浓度的MnSO4·H2O溶液,浓度优选3%;4%~10%摩尔浓度的NaCl溶液,浓度优选7%。为方便起见,以下浓度均为摩尔浓度。In this step, the formula for preparing the mixed solution of hydrated manganese oxide seed crystals can be: KMnO 4 solution with a molar concentration of 0.1% to 0.5%, preferably 0.4%; MnSO 4 ·H 2 O solution with a molar concentration of 2% to 5% , the concentration is preferably 3%; 4% to 10% molar concentration of NaCl solution, the concentration is preferably 7%. For convenience, the following concentrations are molar concentrations.
且在上述配方的前提下,所述MnSO4·H2O溶液与所述NaCl溶液的体积比为5:1~2:1之间,优选3:1;且所述混合液Ⅰ与KMnO4溶液的体积比介于4:1~1:1之间,优选2:1。And under the premise of the above formula, the volume ratio of the MnSO 4 ·H 2 O solution to the NaCl solution is between 5:1 and 2:1, preferably 3:1; and the mixed solution I and KMnO 4 The volume ratio of the solution is between 4:1 and 1:1, preferably 2:1.
上述设定的反应条件为:温度介于90~100℃之间,搅拌反应时间介于1.5~3h之间,优选2h。The reaction conditions set above are as follows: the temperature is between 90-100° C., and the stirring reaction time is between 1.5-3 hours, preferably 2 hours.
步骤12:对所述水合二氧化锰晶种混合液进行稀土掺杂晶粒放大处理;Step 12: performing rare earth-doped crystal grain enlargement treatment on the hydrated manganese dioxide seed mixture;
在该步骤中,具体操作为:采用0.2%~1%的CeCl3(氯化铈)溶液与2%~5%的MnSO4·H2O溶液,按照一定的体积比配制成混合液Ⅱ,将所述混合液Ⅱ与所述水合二氧化锰晶种混合液按照一定的体积比混合,配制成混合液Ⅲ,再向所述混合液Ⅲ中加入1%~3%KMnO4溶液,在20~40℃条件下,将混合溶液搅拌反应1.5~3h,得到稀土掺杂水合氧化锰混合液;In this step, the specific operation is: use 0.2%-1% CeCl 3 (cerium chloride) solution and 2%-5% MnSO 4 ·H 2 O solution to prepare mixed solution II according to a certain volume ratio, Mix the mixed solution II with the hydrated manganese dioxide seed mixed solution according to a certain volume ratio to prepare mixed solution III, then add 1% to 3 % KMnO4 solution to the mixed solution III, at 20 Under the condition of ~40°C, the mixed solution is stirred and reacted for 1.5-3 hours to obtain the rare earth-doped hydrated manganese oxide mixed solution;
在上述过程中,所采用的MnSO4·H2O溶液的浓度优选为3%,所采用的CeCl3溶液的浓度优选0.7%,且所述MnSO4·H2O溶液与CeCl3溶液按照8:1~12:1的体积比配制成混合液Ⅱ,优选为10:1。In the above process, the concentration of the MnSO 4 ·H 2 O solution used is preferably 3%, the concentration of the CeCl 3 solution used is preferably 0.7%, and the MnSO 4 ·H 2 O solution and the CeCl 3 solution are in accordance with 8 : The volume ratio of 1 to 12:1 is prepared into the mixed solution II, preferably 10:1.
且所述混合液Ⅱ与所述水合二氧化锰晶种混合液的体积比为3:1~5:1之间,优选为4:1;在所述混合液Ⅲ中所加入的KMnO4溶液的摩尔浓度优选为2%,所述混合液Ⅲ与所述KMnO4溶液的体积比为3:1~1:1之间,优选为2:1。And the volume ratio of the mixed solution II to the hydrated manganese dioxide seed mixed solution is between 3:1 and 5:1, preferably 4 :1; the KMnO solution added in the mixed solution III The molar concentration of is preferably 2%, and the volume ratio of the mixed solution III to the KMnO 4 solution is between 3:1 and 1:1, preferably 2:1.
另外,在进行稀土掺杂晶粒放大处理的过程中,所述混合溶液搅拌反应的时间介于1.5~3h之间,优选2h;且反应温度介于20~40℃之间。In addition, during the rare earth-doped grain enlargement process, the time for stirring and reacting the mixed solution is between 1.5-3 hours, preferably 2 hours; and the reaction temperature is between 20-40°C.
步骤13:对所述稀土掺杂水合氧化锰混合液进行沉淀物粒径分级处理,取粒径大于10μm的沉淀物进行压滤处理,收集压滤处理后得到的吸附剂滤饼;Step 13: performing sediment particle size classification treatment on the rare earth-doped hydrated manganese oxide mixed solution, taking sediments with a particle size greater than 10 μm for pressure filtration treatment, and collecting the adsorbent filter cake obtained after the pressure filtration treatment;
在该步骤中,可以采用水力旋流器对稀土掺杂水合氧化锰混合液进行沉淀物粒径分级处理,选取粒径大于10μm的沉淀物进入压滤机,再进行压滤脱水处理,得到吸附剂滤饼。In this step, a hydrocyclone can be used to classify the rare earth-doped manganese oxide hydrate mixed solution for sediment particle size classification, and select the precipitate with a particle size larger than 10 μm to enter the filter press, and then perform press filter dehydration treatment to obtain adsorption agent filter cake.
步骤14:将所述吸附剂滤饼在50℃~75℃条件下干燥1.5h~3h,至表面无明显水分,得到最终的稀土掺杂水合氧化锰的吸附剂。Step 14: drying the filter cake of the adsorbent at 50° C. to 75° C. for 1.5 h to 3 h until there is no obvious moisture on the surface to obtain the final rare earth-doped hydrated manganese oxide adsorbent.
采用上述步骤所制备的稀土掺杂水合氧化锰吸附剂能够应用于废水中铊、镉、铅等重金属的深度吸附去除。The rare earth-doped hydrated manganese oxide adsorbent prepared by the above steps can be applied to deep adsorption and removal of heavy metals such as thallium, cadmium and lead in wastewater.
综上所述,本发明实施例所提供的制备方法具有如下的优点和意义:In summary, the preparation method provided by the embodiments of the present invention has the following advantages and significance:
(1)通过晶种制备与稀土掺杂晶粒放大两步处理,实现了纳米金属氧化物的粒径在一定范围内的可控增长,使得制得的稀土掺杂水合氧化锰吸附剂作为一种投加型吸附剂在完成吸附废水中重金属过程后,能够从废水中沉淀分离,提高了其工程应用价值。(1) Through the two-step process of seed crystal preparation and rare earth-doped grain amplification, the particle size of nano-metal oxides can be controlled within a certain range. After completing the process of adsorbing heavy metals in wastewater, the dosing-type adsorbent can be precipitated and separated from wastewater, which improves its engineering application value.
(2)采用氯化铈掺杂,提高了传统水合氧化锰的选择吸附性,能够用于废水中微量的Tl、Hg等重金属的去除。(2) Doping with cerium chloride improves the selective adsorption of traditional hydrated manganese oxide, and can be used to remove trace amounts of heavy metals such as Tl and Hg in wastewater.
(3)由于该吸附剂的吸附反应速度快、吸附容量高,从而减少其在废水处理过程中的投加量,降低了废水处理的运行成本。(3) Due to the fast adsorption reaction speed and high adsorption capacity of the adsorbent, its dosage in the wastewater treatment process is reduced, and the operating cost of wastewater treatment is reduced.
以上所述,仅为本发明较佳的具体实施方式,但本发明的保护范围并不局限于此,任何熟悉本技术领域的技术人员在本发明披露的技术范围内,可轻易想到的变化或替换,都应涵盖在本发明的保护范围之内。因此,本发明的保护范围应该以权利要求书的保护范围为准。The above is only a preferred embodiment of the present invention, but the scope of protection of the present invention is not limited thereto. Any person familiar with the technical field can easily conceive of changes or changes within the technical scope disclosed in the present invention. Replacement should be covered within the protection scope of the present invention. Therefore, the protection scope of the present invention should be determined by the protection scope of the claims.
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