CN110180492A - A kind of active filter and its preparation method and application for removing magnesium ion - Google Patents
A kind of active filter and its preparation method and application for removing magnesium ion Download PDFInfo
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- CN110180492A CN110180492A CN201910309803.8A CN201910309803A CN110180492A CN 110180492 A CN110180492 A CN 110180492A CN 201910309803 A CN201910309803 A CN 201910309803A CN 110180492 A CN110180492 A CN 110180492A
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- JLVVSXFLKOJNIY-UHFFFAOYSA-N Magnesium ion Chemical compound [Mg+2] JLVVSXFLKOJNIY-UHFFFAOYSA-N 0.000 title claims abstract description 49
- 229910001425 magnesium ion Inorganic materials 0.000 title claims abstract description 49
- 238000002360 preparation method Methods 0.000 title claims description 15
- 239000000047 product Substances 0.000 claims abstract description 58
- 238000003756 stirring Methods 0.000 claims abstract description 25
- 239000012065 filter cake Substances 0.000 claims abstract description 22
- 238000000034 method Methods 0.000 claims abstract description 13
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 claims description 99
- 239000000203 mixture Substances 0.000 claims description 23
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 claims description 18
- WMFOQBRAJBCJND-UHFFFAOYSA-M Lithium hydroxide Chemical compound [Li+].[OH-] WMFOQBRAJBCJND-UHFFFAOYSA-M 0.000 claims description 15
- 239000006004 Quartz sand Substances 0.000 claims description 15
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 claims description 15
- MUBZPKHOEPUJKR-UHFFFAOYSA-N Oxalic acid Chemical compound OC(=O)C(O)=O MUBZPKHOEPUJKR-UHFFFAOYSA-N 0.000 claims description 9
- 239000012153 distilled water Substances 0.000 claims description 8
- 238000004056 waste incineration Methods 0.000 claims description 8
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 8
- KRHYYFGTRYWZRS-UHFFFAOYSA-N Fluorane Chemical compound F KRHYYFGTRYWZRS-UHFFFAOYSA-N 0.000 claims description 6
- TWRXJAOTZQYOKJ-UHFFFAOYSA-L Magnesium chloride Chemical compound [Mg+2].[Cl-].[Cl-] TWRXJAOTZQYOKJ-UHFFFAOYSA-L 0.000 claims description 6
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 claims description 6
- KWYUFKZDYYNOTN-UHFFFAOYSA-M Potassium hydroxide Chemical compound [OH-].[K+] KWYUFKZDYYNOTN-UHFFFAOYSA-M 0.000 claims description 5
- 239000000945 filler Substances 0.000 claims description 5
- 239000002253 acid Substances 0.000 claims description 4
- 229910001629 magnesium chloride Inorganic materials 0.000 claims description 3
- 235000006408 oxalic acid Nutrition 0.000 claims description 3
- 238000001914 filtration Methods 0.000 claims 2
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 claims 1
- 239000006227 byproduct Substances 0.000 claims 1
- 230000005611 electricity Effects 0.000 claims 1
- 229910052739 hydrogen Inorganic materials 0.000 claims 1
- 239000001257 hydrogen Substances 0.000 claims 1
- 239000000463 material Substances 0.000 abstract description 28
- CSNNHWWHGAXBCP-UHFFFAOYSA-L Magnesium sulfate Chemical compound [Mg+2].[O-][S+2]([O-])([O-])[O-] CSNNHWWHGAXBCP-UHFFFAOYSA-L 0.000 abstract description 26
- 229910052943 magnesium sulfate Inorganic materials 0.000 abstract description 13
- 235000019341 magnesium sulphate Nutrition 0.000 abstract description 13
- 239000003513 alkali Substances 0.000 abstract description 9
- 239000002245 particle Substances 0.000 abstract description 9
- 238000002791 soaking Methods 0.000 abstract description 4
- 238000002156 mixing Methods 0.000 abstract description 3
- 238000005406 washing Methods 0.000 abstract description 3
- 230000009286 beneficial effect Effects 0.000 abstract description 2
- 239000013078 crystal Substances 0.000 abstract description 2
- 238000001035 drying Methods 0.000 abstract description 2
- 239000000243 solution Substances 0.000 description 76
- 238000006243 chemical reaction Methods 0.000 description 7
- 238000010248 power generation Methods 0.000 description 7
- 230000000694 effects Effects 0.000 description 5
- 239000010802 sludge Substances 0.000 description 3
- FYYHWMGAXLPEAU-UHFFFAOYSA-N Magnesium Chemical compound [Mg] FYYHWMGAXLPEAU-UHFFFAOYSA-N 0.000 description 2
- 229910019440 Mg(OH) Inorganic materials 0.000 description 2
- 239000012670 alkaline solution Substances 0.000 description 2
- 239000011777 magnesium Substances 0.000 description 2
- 229910052749 magnesium Inorganic materials 0.000 description 2
- 239000011148 porous material Substances 0.000 description 2
- BPQQTUXANYXVAA-UHFFFAOYSA-N Orthosilicate Chemical compound [O-][Si]([O-])([O-])[O-] BPQQTUXANYXVAA-UHFFFAOYSA-N 0.000 description 1
- 229910021536 Zeolite Inorganic materials 0.000 description 1
- 230000002378 acidificating effect Effects 0.000 description 1
- 239000003463 adsorbent Substances 0.000 description 1
- 238000005273 aeration Methods 0.000 description 1
- 238000001354 calcination Methods 0.000 description 1
- 239000000149 chemical water pollutant Substances 0.000 description 1
- 238000005345 coagulation Methods 0.000 description 1
- 230000015271 coagulation Effects 0.000 description 1
- HNPSIPDUKPIQMN-UHFFFAOYSA-N dioxosilane;oxo(oxoalumanyloxy)alumane Chemical compound O=[Si]=O.O=[Al]O[Al]=O HNPSIPDUKPIQMN-UHFFFAOYSA-N 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 230000003203 everyday effect Effects 0.000 description 1
- 238000011049 filling Methods 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 238000007654 immersion Methods 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000011159 matrix material Substances 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 244000005700 microbiome Species 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012544 monitoring process Methods 0.000 description 1
- 238000011056 performance test Methods 0.000 description 1
- 238000001556 precipitation Methods 0.000 description 1
- 238000009287 sand filtration Methods 0.000 description 1
- 239000010865 sewage Substances 0.000 description 1
- 238000001179 sorption measurement Methods 0.000 description 1
- 239000006228 supernatant Substances 0.000 description 1
- 239000010457 zeolite Substances 0.000 description 1
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
- B01J20/02—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material
- B01J20/10—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material comprising silica or silicate
- B01J20/103—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material comprising silica or silicate comprising silica
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/28—Treatment of water, waste water, or sewage by sorption
- C02F1/281—Treatment of water, waste water, or sewage by sorption using inorganic sorbents
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2103/00—Nature of the water, waste water, sewage or sludge to be treated
- C02F2103/06—Contaminated groundwater or leachate
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W10/00—Technologies for wastewater treatment
- Y02W10/10—Biological treatment of water, waste water, or sewage
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- Chemical & Material Sciences (AREA)
- Inorganic Chemistry (AREA)
- Organic Chemistry (AREA)
- Life Sciences & Earth Sciences (AREA)
- Hydrology & Water Resources (AREA)
- Engineering & Computer Science (AREA)
- Environmental & Geological Engineering (AREA)
- Water Supply & Treatment (AREA)
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- Chemical Kinetics & Catalysis (AREA)
- Filtering Materials (AREA)
- Processing Of Solid Wastes (AREA)
Abstract
本发明属于活性滤料技术领域,具体涉及一种用于去除镁离子的活性滤料制备方法包括如下步骤,S1、将石英砂与质量浓度为10%‑15%的酸溶液按照质量比为(1‑2):1均匀混合,搅拌处理40‑50h,过滤,将滤饼取出并干燥,得到产物A;S2、将产物A与质量浓度为10%‑15%的碱溶液一按照质量比为1:(1‑1.5)均匀混合,搅拌处理40‑50h,得到产物B;S3、将产物B与质量浓度为10%‑12%的镁离子溶液按照质量比为1:(1‑1.8)均匀混合,搅拌浸泡2‑4h后添加质量浓度为12%‑16%的碱溶液二,得到产物C;S4、洗去产物C表面残留的硫酸镁溶液、碱溶液二,干燥后得到活性滤料。本发明的有益效果是:本发明得到的活性滤料粒度较细,呈现无色晶体状态,对镁离子去除迅速且高效。The invention belongs to the technical field of active filter materials, and in particular relates to a method for preparing an active filter material for removing magnesium ions. 1-2): 1 is uniformly mixed, stirred for 40-50h, filtered, and the filter cake is taken out and dried to obtain product A; S2, product A and mass concentration are 10%-15% alkaline solution—according to mass ratio, 1: (1-1.5) uniform mixing, stirring for 40-50h, to obtain product B; S3, be that the magnesium ion solution of 10%-12% with product B and mass concentration is 1: (1-1.8) uniform according to mass ratio Mixing, stirring and soaking for 2-4h, adding alkali solution II with a mass concentration of 12%-16% to obtain product C; S4, washing off residual magnesium sulfate solution and alkali solution II on the surface of product C, and drying to obtain an active filter material. The beneficial effects of the present invention are: the particle size of the active filter material obtained by the present invention is relatively fine, showing a colorless crystal state, and the removal of magnesium ions is rapid and efficient.
Description
技术领域technical field
本发明属于活性滤料技术领域,具体涉及一种用于去除镁离子的活性滤料及其制备方法和应用。The invention belongs to the technical field of active filter materials, and in particular relates to an active filter material for removing magnesium ions and a preparation method and application thereof.
背景技术Background technique
目前各污水处理厂监测表明垃圾焚烧发电渗滤液中镁离子含量较高,镁虽然是人体生长的必须元素,但高浓度的镁离子会给生产和生活带来一些弊端。例如含高镁离子的出水在回用时会使管道内结垢从而堵塞管道,此外高镁离子的垃圾焚烧发电渗滤液会对活性污泥中的微生物产生抑制作用从而影响出水水质。At present, the monitoring of various sewage treatment plants shows that the content of magnesium ions in the leachate of waste incineration power generation is relatively high. Although magnesium is an essential element for human growth, high concentrations of magnesium ions will bring some disadvantages to production and life. For example, when the effluent containing high magnesium ions is reused, it will cause scaling in the pipeline and block the pipeline. In addition, the leachate of waste incineration power generation with high magnesium ions will inhibit the microorganisms in the activated sludge and affect the quality of the effluent.
目前,垃圾焚烧发电渗滤液镁离子去除的方法也有不少,例如生物吸附剂法,活性污泥法。生物吸附剂法对镁离子的去除效果较好,但去除效果不稳定会受到一些外界环境因素的影响(初始镁离子浓度,搅拌速度);活性污泥法对镁离子的去除迅速且高效,但易受到溶液pH的影响。At present, there are many methods for removing magnesium ions from leachate of waste incineration power generation, such as biological adsorbent method and activated sludge method. The biosorbent method has a better removal effect of magnesium ions, but the removal effect is unstable and will be affected by some external environmental factors (initial magnesium ion concentration, stirring speed); the activated sludge method can remove magnesium ions quickly and efficiently, but Susceptible to solution pH.
发明内容SUMMARY OF THE INVENTION
为了解决上述问题,本发明提供一种用于去除镁离子的活性滤料的制备方法,通过该方法制备的活性滤料去除镁离子稳定且高效。In order to solve the above problems, the present invention provides a method for preparing an active filter material for removing magnesium ions, and the active filter material prepared by the method is stable and efficient in removing magnesium ions.
本发明提供了如下的技术方案:The present invention provides the following technical solutions:
一种用于去除镁离子的活性滤料的制备方法,包括如下步骤,A preparation method for an active filter material for removing magnesium ions, comprising the steps,
S1、将石英砂与质量浓度为10%-15%的酸溶液按照质量比为(1-2):1均匀混合,搅拌处理40-50h,过滤,将滤饼取出并干燥,得到产物A;S1, the quartz sand and the acid solution with mass concentration of 10%-15% are uniformly mixed according to the mass ratio of (1-2): 1, stirred for 40-50h, filtered, and the filter cake is taken out and dried to obtain product A;
S2、将产物A与质量浓度为10%-15%的碱溶液一按照质量比为1:(1-1.5)均匀混合,搅拌处理40-50h,过滤,将滤饼取出并干燥,然后在300-500℃下煅烧3-5h,冷却至20-30℃,得到产物B;S2, product A is uniformly mixed with the alkali solution whose mass concentration is 10%-15% according to the mass ratio of 1:(1-1.5), stirred for 40-50h, filtered, and the filter cake is taken out and dried, then at 300 Calcined at -500°C for 3-5h, cooled to 20-30°C to obtain product B;
S3、将产物B与质量浓度为10%-12%的镁离子溶液按照质量比为1:(1-1.8)均匀混合,搅拌浸泡2-4h后添加质量浓度为12%-16%的碱溶液二,控制pH为9-10,在20-30℃搅拌反应1-2h,过滤,将滤饼取出,得到产物C;S3, the product B and the magnesium ion solution with a mass concentration of 10%-12% are uniformly mixed according to the mass ratio of 1: (1-1.8), and the alkali solution with a mass concentration of 12%-16% is added after stirring and soaking for 2-4h 2. Control the pH to be 9-10, stir and react at 20-30 ° C for 1-2 h, filter, and take out the filter cake to obtain product C;
S4、洗去产物C表面残留的镁离子溶液、碱溶液二,干燥后得到活性滤料。S4, washing off the residual magnesium ion solution and alkali solution 2 on the surface of the product C, and drying to obtain an active filter material.
优选的,所述S2中,在将产物A与质量浓度为10%-15%的碱溶液一按照质量比为1:(1-1.5)均匀混合之前,首先使用质量浓度为1%-3%的碱溶液一对产物A洗涤2-4次,每次3-5min。Preferably, in the S2, before uniformly mixing the product A with the alkali solution with a mass concentration of 10%-15% according to a mass ratio of 1:(1-1.5), first use a mass concentration of 1%-3% The alkaline solution of the product A was washed 2-4 times for 3-5 min each time.
优选的,所述S1中,酸溶液选自盐酸溶液、硫酸溶液、草酸溶液、氢氟酸溶液中的任意一种或任意几种的混合物;Preferably, in the S1, the acid solution is selected from any one or a mixture of any of a hydrochloric acid solution, a sulfuric acid solution, an oxalic acid solution, and a hydrofluoric acid solution;
所述S2中,碱溶液一选自氢氧化钠溶液、氢氧化钾溶液、氢氧化锂溶液中的任意一种或任意几种的混合物;In described S2, alkali solution—is selected from any one or any mixture of several in sodium hydroxide solution, potassium hydroxide solution, lithium hydroxide solution;
所述S3中,碱溶液二选自氢氧化钠溶液、氢氧化钾溶液、氢氧化锂溶液中的任意一种或任意几种的混合物。In the S3, the alkali solution II is selected from any one or a mixture of any of the sodium hydroxide solution, potassium hydroxide solution, and lithium hydroxide solution.
优选的,所述S3中,镁离子溶液为硫酸镁溶液或者氯化镁溶液。Preferably, in the S3, the magnesium ion solution is a magnesium sulfate solution or a magnesium chloride solution.
优选的,所述S4中洗去产物C表面残留的镁离子溶液、碱溶液二的方法为先用质量浓度为1%-3%的氢氧化钠溶液洗涤1-3次,每次3-5min,再用蒸馏水洗涤2-4次,每次3-5min。Preferably, the method of washing off the residual magnesium ion solution and alkali solution 2 on the surface of product C in S4 is to first wash 1-3 times with sodium hydroxide solution with a mass concentration of 1%-3%, each time 3-5min , and then washed with distilled water 2-4 times, each 3-5min.
优选的,所述石英砂的粒径为1.2-1.5mm。Preferably, the particle size of the quartz sand is 1.2-1.5 mm.
本发明还提供一种活性填料,通过上述任一项所述的方法进行制备。The present invention also provides an active filler, which is prepared by any of the methods described above.
本发明的活性填料用于去除垃圾焚烧发电渗滤液中的镁离子。The active filler of the present invention is used for removing magnesium ions in the leachate of waste incineration power generation.
本发明的有益效果是:The beneficial effects of the present invention are:
1、本发明通过将石英砂依次在酸性、碱性条件下进行刻蚀处理,碱性条件下使得使镁离子转化为Mg(OH)2沉淀并吸附在石英砂表面获得活性滤料,得到的活性滤料粒度较细,呈现无色晶体状态,对镁离子去除迅速且高效。1. In the present invention, the quartz sand is successively etched under acidic and alkaline conditions, and under alkaline conditions, magnesium ions are converted into Mg(OH) 2 to precipitate and adsorb on the surface of the quartz sand to obtain an active filter material. The particle size of the active filter material is fine, showing a colorless crystal state, and the removal of magnesium ions is rapid and efficient.
2、该制备方法在常温即可,无需加热,整个操作简单。2. The preparation method can be performed at room temperature without heating, and the whole operation is simple.
3、本发明制备的活性滤料,可以有效的降低垃圾焚烧发电渗滤液中的镁离子浓度,镁离子的去除率均在80%以上,其中效果最好的活性填料,镁离子去除率可达到了90.2%。3. The active filter material prepared by the present invention can effectively reduce the concentration of magnesium ions in the leachate of waste incineration power generation, and the removal rate of magnesium ions is above 80%. up 90.2%.
具体实施方式Detailed ways
下面结合具体实施例对本发明做具体说明。The present invention will be specifically described below with reference to specific embodiments.
实施例1Example 1
一种用于去除镁离子的活性滤料的制备方法,包括如下步骤,A preparation method for an active filter material for removing magnesium ions, comprising the steps,
S1、将粒径为1.2mm的石英砂与质量浓度为10%的盐酸溶液按照质量比为1:1均匀混合,搅拌处理40h,过滤,将滤饼取出并干燥,得到产物A;S1, uniformly mix quartz sand with a particle size of 1.2mm and a hydrochloric acid solution with a mass concentration of 10% according to a mass ratio of 1:1, stir for 40h, filter, take out the filter cake and dry to obtain product A;
S2、使用质量浓度为1%的氢氧化钠溶液对产物A洗涤2次,每次5min,将洗涤后的产物A与质量浓度为10%的氢氧化钠溶液按照质量比为1:1均匀混合,搅拌处理40h,过滤,将滤饼取出并干燥,然后在300℃下煅烧5h,冷却至20℃,得到产物B;S2. Use the sodium hydroxide solution with a mass concentration of 1% to wash the product A twice, 5 minutes each time, and mix the washed product A with a sodium hydroxide solution with a mass concentration of 10% according to a mass ratio of 1:1. , stirred for 40h, filtered, the filter cake was taken out and dried, then calcined at 300°C for 5h, cooled to 20°C to obtain product B;
S3、将产物B与质量浓度为10%的硫酸镁溶液按照质量比为1:1均匀混合,搅拌浸泡2h后添加质量浓度为12%的氢氧化钠溶液,控制pH为9,在20℃搅拌反应1h,过滤,将滤饼取出,得到产物C;S3. Mix the product B and the magnesium sulfate solution with a mass concentration of 10% uniformly according to a mass ratio of 1:1, stir and soak for 2 hours, add a sodium hydroxide solution with a mass concentration of 12%, control the pH to be 9, and stir at 20 °C The reaction was carried out for 1 h, filtered, and the filter cake was taken out to obtain product C;
S4、先用质量浓度为1%的氢氧化钠溶液洗涤1次,每次3min,再用蒸馏水洗涤2次,每次3min,洗去产物C表面残留的硫酸镁溶液、氢氧化钠溶液,干燥后得到活性滤料。S4, first wash once with 1% sodium hydroxide solution, each time for 3 minutes, then wash with distilled water twice, each time for 3 minutes, wash away the residual magnesium sulfate solution and sodium hydroxide solution on the surface of product C, and dry Then the active filter material is obtained.
实施例2Example 2
一种用于去除镁离子的活性滤料的制备方法,包括如下步骤,A preparation method for an active filter material for removing magnesium ions, comprising the steps,
S1、将粒径为1.4mm石英砂与质量浓度为12%的盐酸溶液按照质量比为1.5:1均匀混合,搅拌处理48h,过滤,将滤饼取出并干燥,得到产物A;S1, uniformly mix the quartz sand with a particle size of 1.4mm and a hydrochloric acid solution with a mass concentration of 12% according to a mass ratio of 1.5:1, stir for 48h, filter, take out the filter cake and dry to obtain product A;
S2、使用质量浓度为2%的氢氧化钠溶液对产物A洗涤3次,每次4min,将洗涤后的产物A与质量浓度为12%的氢氧化钠溶液按照质量比为1:1.2均匀混合,搅拌处理48h,过滤,将滤饼取出并干燥,然后在400℃下煅烧4h,冷却至25℃,得到产物B;S2. Use a sodium hydroxide solution with a mass concentration of 2% to wash the product A for 3 times, 4 minutes each time, and mix the washed product A with a sodium hydroxide solution with a mass concentration of 12% according to a mass ratio of 1:1.2. , stirred for 48h, filtered, the filter cake was taken out and dried, then calcined at 400°C for 4h, cooled to 25°C to obtain product B;
S3、将产物B与质量浓度为11%的硫酸镁溶液按照质量比为1:1.4均匀混合,搅拌浸泡3h后添加质量浓度为14%的氢氧化钠溶液,控制pH为9,在25℃搅拌反应1h,过滤,将滤饼取出,得到产物C;S3. Mix the product B and the magnesium sulfate solution with a mass concentration of 11% uniformly according to a mass ratio of 1:1.4, stir and soak for 3 hours, add a sodium hydroxide solution with a mass concentration of 14%, control the pH to 9, and stir at 25 ° C The reaction was carried out for 1 h, filtered, and the filter cake was taken out to obtain product C;
S4、先用质量浓度为1%-3%的氢氧化钠溶液洗涤2次,每次4min,再用蒸馏水洗涤3次,每次4min,洗去产物C表面残留的硫酸镁溶液、氢氧化钠溶液,干燥后得到活性滤料。S4, first wash 2 times with a sodium hydroxide solution with a mass concentration of 1%-3%, each 4min, and then wash with distilled water 3 times, each 4min, wash away the residual magnesium sulfate solution and sodium hydroxide on the surface of product C The solution is dried to obtain an active filter material.
实施例3Example 3
一种用于去除镁离子的活性滤料的制备方法,包括如下步骤,A preparation method for an active filter material for removing magnesium ions, comprising the steps,
S1、将粒径为1.2mm石英砂与质量浓度为10%的盐酸溶液按照质量比为1.5:1均匀混合,搅拌处理50h,过滤,将滤饼取出并干燥,得到产物A;S1, uniformly mix quartz sand with a particle size of 1.2 mm and a hydrochloric acid solution with a mass concentration of 10% according to a mass ratio of 1.5:1, stir for 50h, filter, take out the filter cake and dry to obtain product A;
S2、使用质量浓度为3%的氢氧化钠溶液对产物A洗涤2次,每次3min,将洗涤后的产物A与质量浓度为10的氢氧化钠溶液按照质量比为1:1.3均匀混合,搅拌处理40h,过滤,将滤饼取出并干燥,然后在500℃下煅烧5h,冷却至20℃,得到产物B;S2, using the sodium hydroxide solution with a mass concentration of 3% to wash the product A twice, 3min each time, the washed product A and the sodium hydroxide solution with a mass concentration of 10 are uniformly mixed according to a mass ratio of 1:1.3, Stir for 40h, filter, take out the filter cake and dry, then calcinate at 500°C for 5h, and cool to 20°C to obtain product B;
S3、将产物B与质量浓度为12%的硫酸镁溶液按照质量比为1:1.6均匀混合,搅拌浸泡4h后添加质量浓度为14%的氢氧化钠溶液,控制pH为9,在30℃搅拌反应1h,过滤,将滤饼取出,得到产物C;S3. Mix the product B and the magnesium sulfate solution with a mass concentration of 12% uniformly according to the mass ratio of 1:1.6. After stirring and soaking for 4 hours, add a sodium hydroxide solution with a mass concentration of 14%, control the pH to 9, and stir at 30 ° C. The reaction was carried out for 1 h, filtered, and the filter cake was taken out to obtain product C;
S4、先用质量浓度为1%的氢氧化钠溶液洗涤1次,每次3min,再用蒸馏水洗涤2次,每次5min,洗去产物C表面残留的硫酸镁溶液、氢氧化钠溶液,干燥后得到活性滤料。S4, first wash once with 1% sodium hydroxide solution for 3 minutes each time, then wash with distilled water twice for 5 minutes each time, wash away the residual magnesium sulfate solution and sodium hydroxide solution on the surface of product C, and dry Then the active filter material is obtained.
实施例4Example 4
一种用于去除镁离子的活性滤料的制备方法,包括如下步骤,A preparation method for an active filter material for removing magnesium ions, comprising the steps,
S1、将粒径为1.2mm石英砂与质量浓度为15%的盐酸溶液按照质量比为1.2:1均匀混合,搅拌处理40h,过滤,将滤饼取出并干燥,得到产物A;S1, uniformly mix the quartz sand with a particle size of 1.2mm and a hydrochloric acid solution with a mass concentration of 15% according to a mass ratio of 1.2:1, stir for 40h, filter, take out the filter cake and dry to obtain product A;
S2、使用质量浓度为1%%的氢氧化钠溶液对产物A洗涤4次,每次5min,将洗涤后的产物A与质量浓度为15%的氢氧化钠溶液按照质量比为1:1.5均匀混合,搅拌处理50h,过滤,将滤饼取出并干燥,然后在500℃下煅烧5h,冷却至30℃,得到产物B;S2. Use the sodium hydroxide solution with a mass concentration of 1% to wash the product A for 4 times, 5 minutes each time, and the washed product A and the sodium hydroxide solution with a mass concentration of 15% are uniformly 1:1.5 in mass ratio Mixed, stirred for 50 hours, filtered, the filter cake was taken out and dried, then calcined at 500 °C for 5 hours, cooled to 30 °C to obtain product B;
S3、将产物B与质量浓度为10%的硫酸镁溶液按照质量比为1:1.5均匀混合,搅拌浸泡4h后添加质量浓度为14%的氢氧化钠溶液,控制pH为10,在30℃搅拌反应1-2h,过滤,将滤饼取出,得到产物C;S3. The product B is uniformly mixed with the magnesium sulfate solution with a mass concentration of 10% according to the mass ratio of 1:1.5. After stirring and soaking for 4 hours, a sodium hydroxide solution with a mass concentration of 14% is added, and the pH is controlled to be 10. Stir at 30 °C The reaction was carried out for 1-2h, filtered, and the filter cake was taken out to obtain product C;
S4、先用质量浓度为3%的氢氧化钠溶液洗涤1次,每次5min,再用蒸馏水洗涤2次,每次5min,洗去产物C表面残留的硫酸镁溶液、氢氧化钠溶液,干燥后得到活性滤料。S4, first wash once with 3% sodium hydroxide solution, each time for 5 minutes, then wash with distilled water twice, each time for 5 minutes, wash away the residual magnesium sulfate solution and sodium hydroxide solution on the surface of product C, and dry Then the active filter material is obtained.
实施例5Example 5
一种用于去除镁离子的活性滤料的制备方法,包括如下步骤,A preparation method for an active filter material for removing magnesium ions, comprising the steps,
S1、将粒径为1.5mm石英砂与质量浓度为15%的盐酸溶液按照质量比为2:1均匀混合,搅拌处理50h,过滤,将滤饼取出并干燥,得到产物A;S1, uniformly mix quartz sand with a particle size of 1.5mm and a hydrochloric acid solution with a mass concentration of 15% according to a mass ratio of 2:1, stir for 50h, filter, take out the filter cake and dry to obtain product A;
S2、使用质量浓度为3%的氢氧化钠溶液对产物A洗涤4次,每次5min,将洗涤后的产物A与质量浓度为15%的氢氧化钠溶液按照质量比为1:1.5均匀混合,搅拌处理50h,过滤,将滤饼取出并干燥,然后在500℃下煅烧5h,冷却至30℃,得到产物B;S2. Use the sodium hydroxide solution with a mass concentration of 3% to wash the product A for 4 times, 5 minutes each time, and uniformly mix the washed product A and the sodium hydroxide solution with a mass concentration of 15% according to a mass ratio of 1:1.5 , stirred for 50h, filtered, the filter cake was taken out and dried, then calcined at 500°C for 5h, cooled to 30°C to obtain product B;
S3、将产物B与质量浓度为12%的硫酸镁溶液按照质量比为1:1.8均匀混合,搅拌浸泡4h后添加质量浓度为16%的氢氧化钠溶液,控制pH为10,在30℃搅拌反应2h,过滤,将滤饼取出,得到产物C;S3. Mix the product B and the magnesium sulfate solution with a mass concentration of 12% uniformly according to a mass ratio of 1:1.8, stir and soak for 4 hours, add a sodium hydroxide solution with a mass concentration of 16%, control the pH to be 10, and stir at 30 °C The reaction was carried out for 2h, filtered, and the filter cake was taken out to obtain product C;
S4、先用质量浓度为3%的氢氧化钠溶液洗涤3次,每次5min,再用蒸馏水洗涤4次,每次5min,洗去产物C表面残留的硫酸镁溶液、氢氧化钠溶液,干燥后得到活性滤料。S4, first wash 3 times with 3% sodium hydroxide solution, each 5min, then wash 4 times with distilled water, 5min each time, wash away the residual magnesium sulfate solution and sodium hydroxide solution on the surface of product C, and dry Then the active filter material is obtained.
本发明实施例1-5中,硫酸镁溶液可以替换为氯化镁溶液;In the embodiment of the present invention 1-5, magnesium sulfate solution can be replaced with magnesium chloride solution;
盐酸溶液可以替换为盐酸溶液、硫酸溶液、草酸溶液、氢氟酸溶液中的任意一种或任意几种的混合物;The hydrochloric acid solution can be replaced with any one or any mixture of hydrochloric acid solution, sulfuric acid solution, oxalic acid solution and hydrofluoric acid solution;
氢氧化钠溶液可以替换为氢氧化钠溶液、氢氧化钾溶液、氢氧化锂溶液中的任意一种或任意几种的混合物。The sodium hydroxide solution can be replaced by any one of sodium hydroxide solution, potassium hydroxide solution, and lithium hydroxide solution or a mixture of any of them.
除镁离子性能检测Magnesium removal performance test
将垃圾焚烧发电渗滤液依次经过曝气,混凝,沉淀,石英砂过滤处理后,将上清液引入5个并联的直径为45mm,高为1.2m的反应器内,5个反应器内对应填充实施例1-5制备的活性滤料,填充高度均为0.8m。渗滤液的流量控制在18L/h,连续运行30天,每隔3天使用蒸馏水对活性滤料冲洗一次,每天分别检测5个反应器进水口和出水口的镁离子浓度,结果如下表所示。The leachate of waste incineration power generation is successively treated by aeration, coagulation, precipitation, and quartz sand filtration, and the supernatant is introduced into 5 parallel reactors with a diameter of 45mm and a height of 1.2m. The 5 reactors correspond to The active filter materials prepared in Examples 1-5 were filled, and the filling height was 0.8 m. The flow rate of the leachate was controlled at 18L/h, and it was operated continuously for 30 days. The active filter material was rinsed with distilled water every 3 days. The magnesium ion concentration at the inlet and outlet of the 5 reactors was detected every day. The results are shown in the following table. .
有上表可知,使用本发明制备的活性滤料,可以有效的降低垃圾焚烧发电渗滤液中的镁离子浓度,镁离子的去除率均在80%以上,其中效果最好的是实施例2制备的活性填料,镁离子去除率达到了90.2%,因为石英砂经过酸洗去除表面的金属杂质后,自身的粒度变小,孔隙率变高,基质的比表面积增大,并经过实施例2所对应浓度的碱性溶液浸泡煅烧后,Mg(OH)2的含量也因硅酸盐本身的非沸石类孔道结构的多样性而分布的更加丰富饱满。在实际反应的过程中OH-的浓度过高或过低会导致镁离子流失或反应不完全,从而降低去除率。但实施例2制备的活性滤料在石英砂孔道效应的协助下,充分发挥在垃圾渗滤液中镁离子的吸附作用,以此来提高滤料对镁离子的去除率,使得该实施例中垃圾渗滤液中的镁离子去除率优于其他实施例。As can be seen from the above table, the use of the active filter material prepared by the present invention can effectively reduce the concentration of magnesium ions in the leachate of waste incineration power generation, and the removal rate of magnesium ions is all above 80%, and the best effect is prepared in Example 2. As the active filler, the removal rate of magnesium ions reached 90.2%, because after the quartz sand was pickled to remove the metal impurities on the surface, the particle size of the quartz sand became smaller, the porosity became higher, and the specific surface area of the matrix increased. After immersion and calcination in alkaline solution of corresponding concentration, the content of Mg(OH) 2 is also more abundant and fuller due to the diversity of non-zeolite pore structure of silicate itself. In the actual reaction process, the concentration of OH - is too high or too low, which will lead to loss of magnesium ions or incomplete reaction, thereby reducing the removal rate. However, the active filter material prepared in Example 2 fully exerts the adsorption effect of magnesium ions in the landfill leachate with the assistance of the pore channel effect of quartz sand, thereby improving the removal rate of magnesium ions by the filter material, so that the garbage in this example is The magnesium ion removal rate in the leachate is better than other examples.
以上所述仅为本发明的优选实施例而已,并不用于限制本发明,尽管参照前述实施例对本发明进行了详细的说明,对于本领域的技术人员来说,其依然可以对前述各实施例所记载的技术方案进行修改,或者对其中部分技术特征进行等同替换。凡在本发明的精神和原则之内,所作的任何修改、等同替换、改进等,均应包含在本发明的保护范围之内。The above descriptions are only preferred embodiments of the present invention, and are not intended to limit the present invention. Although the present invention has been described in detail with reference to the foregoing embodiments, those skilled in the art can still understand the foregoing embodiments. The technical solutions described are modified, or some technical features thereof are equivalently replaced. Any modification, equivalent replacement, improvement, etc. made within the spirit and principle of the present invention shall be included within the protection scope of the present invention.
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111675385A (en) * | 2020-06-28 | 2020-09-18 | 山鹰国际控股股份公司 | Method and system for ultrafiltration aeration and alkali addition iron removal |
Citations (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5554005A (en) * | 1978-10-14 | 1980-04-21 | Agency Of Ind Science & Technol | Recovery of magnesium ion |
| CN101757890A (en) * | 2010-02-05 | 2010-06-30 | 淮安金雨阳环保科技有限公司 | Preparation method of attapulgite filter material for selectively absorbing calcium ions and magnesium ions |
| JP2012240017A (en) * | 2011-05-23 | 2012-12-10 | Nittetsu Kankyo Engineering Kk | Treating material of harmful substance, and treating method of harmful substance |
| CN102908978A (en) * | 2012-11-12 | 2013-02-06 | 江西理工大学 | Method for preparing efficient adsorbent through in-situ reaction |
| CN103521169A (en) * | 2013-10-30 | 2014-01-22 | 吉林大学 | Preparing method of potassium permanganate modified manganese removing filter materials |
| CN103785348A (en) * | 2012-10-29 | 2014-05-14 | 日铁住金环境株式会社 | Harmful-substance processing material, its manufacturing method and harmful-substance processing method |
| CN106881062A (en) * | 2015-12-16 | 2017-06-23 | 营口渤海科技有限公司 | A kind of preparation method of the magnesium hydroxide-flyash built agent for processing fluoride waste |
| US20170190604A1 (en) * | 2015-12-31 | 2017-07-06 | Bp Corporation North America Inc. | Use of magnesium hydroxide in the neutralization of pta wastewater |
| WO2018168558A1 (en) * | 2017-03-14 | 2018-09-20 | オルガノ株式会社 | Water treatment method, magnesium agent for water treatment, and method for producing magnesium agent for water treatment |
-
2019
- 2019-04-17 CN CN201910309803.8A patent/CN110180492B/en active Active
Patent Citations (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5554005A (en) * | 1978-10-14 | 1980-04-21 | Agency Of Ind Science & Technol | Recovery of magnesium ion |
| CN101757890A (en) * | 2010-02-05 | 2010-06-30 | 淮安金雨阳环保科技有限公司 | Preparation method of attapulgite filter material for selectively absorbing calcium ions and magnesium ions |
| JP2012240017A (en) * | 2011-05-23 | 2012-12-10 | Nittetsu Kankyo Engineering Kk | Treating material of harmful substance, and treating method of harmful substance |
| CN103785348A (en) * | 2012-10-29 | 2014-05-14 | 日铁住金环境株式会社 | Harmful-substance processing material, its manufacturing method and harmful-substance processing method |
| CN102908978A (en) * | 2012-11-12 | 2013-02-06 | 江西理工大学 | Method for preparing efficient adsorbent through in-situ reaction |
| CN103521169A (en) * | 2013-10-30 | 2014-01-22 | 吉林大学 | Preparing method of potassium permanganate modified manganese removing filter materials |
| CN106881062A (en) * | 2015-12-16 | 2017-06-23 | 营口渤海科技有限公司 | A kind of preparation method of the magnesium hydroxide-flyash built agent for processing fluoride waste |
| US20170190604A1 (en) * | 2015-12-31 | 2017-07-06 | Bp Corporation North America Inc. | Use of magnesium hydroxide in the neutralization of pta wastewater |
| WO2018168558A1 (en) * | 2017-03-14 | 2018-09-20 | オルガノ株式会社 | Water treatment method, magnesium agent for water treatment, and method for producing magnesium agent for water treatment |
Non-Patent Citations (5)
| Title |
|---|
| 付静: "金属盐改性石英砂的制备及其吸附重金属性能研究", 《中国优秀博硕士学位论文全文数据库 工程科技Ⅰ辑》 * |
| 刘建周主编: "《工业催化工程》", 30 June 2018, 中国矿业大学出版社有限责任公司 * |
| 李凯琦等: "《风化型高岭土深加工技术》", 30 June 2017 * |
| 赵大传等: "氢氧化镁对废水中镍(Ⅱ)吸附性能的研究", 《山东建筑大学学报》 * |
| 金松寿: "《有机催化》", 31 December 1986 * |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111675385A (en) * | 2020-06-28 | 2020-09-18 | 山鹰国际控股股份公司 | Method and system for ultrafiltration aeration and alkali addition iron removal |
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