CN106861663A - A kind of micro-fluidic synthesis trace adsorbent for copper-containing wastewater treatment - Google Patents
A kind of micro-fluidic synthesis trace adsorbent for copper-containing wastewater treatment Download PDFInfo
- Publication number
- CN106861663A CN106861663A CN201710128769.5A CN201710128769A CN106861663A CN 106861663 A CN106861663 A CN 106861663A CN 201710128769 A CN201710128769 A CN 201710128769A CN 106861663 A CN106861663 A CN 106861663A
- Authority
- CN
- China
- Prior art keywords
- copper
- micro
- adsorbent
- containing wastewater
- fluidic
- 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.)
- Pending
Links
Classifications
-
- 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
- B01J20/28—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof characterised by their form or physical properties
- B01J20/28014—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof characterised by their form or physical properties characterised by their form
- B01J20/28016—Particle form
- B01J20/28019—Spherical, ellipsoidal or cylindrical
-
- 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
- B01J19/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J19/0093—Microreactors, e.g. miniaturised or microfabricated reactors
-
- 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
- B01J20/22—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising organic material
- B01J20/24—Naturally occurring macromolecular compounds, e.g. humic acids or their derivatives
-
- 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
- B01J20/22—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising organic material
- B01J20/26—Synthetic macromolecular compounds
- B01J20/268—Polymers created by use of a template, e.g. molecularly imprinted polymers
-
- 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
-
- 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
- C02F1/285—Treatment of water, waste water, or sewage by sorption using synthetic organic sorbents
-
- 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
- B01J2220/00—Aspects relating to sorbent materials
- B01J2220/40—Aspects relating to the composition of sorbent or filter aid materials
- B01J2220/44—Materials comprising a mixture of organic materials
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2101/00—Nature of the contaminant
- C02F2101/10—Inorganic compounds
- C02F2101/20—Heavy metals or heavy metal compounds
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Analytical Chemistry (AREA)
- Life Sciences & Earth Sciences (AREA)
- Hydrology & Water Resources (AREA)
- Engineering & Computer Science (AREA)
- Environmental & Geological Engineering (AREA)
- Water Supply & Treatment (AREA)
- Solid-Sorbent Or Filter-Aiding Compositions (AREA)
- Water Treatment By Sorption (AREA)
Abstract
本发明涉及一种用于含铜废水处理的微流控合成印迹吸附剂,其由如下方法制备:将可溶性的铜盐和乙酸溶解在壳聚糖溶液中,铜离子、壳聚糖和乙酸的质量比为1∶(1~5)∶(1~4),加热搅拌得到分散相;再用微流控装置将连续相剪所述分散相,并将形成的微液滴引入到固化液中交联固化;最后将固化好的微液滴使用脱附剂脱附,并洗净、烘干,即制得所需吸附剂。本发明操作简单、成本低,得到的吸附剂对于铜离子有特定的选择吸附性能,吸附速度快、吸附能力高,且可重复使用;使用微流控造粒技术,颗粒粒径均匀,组分、形貌和大小均一,对于含铜离子的工业废水的处理具有深远的研究前景。
The invention relates to a microfluidic synthetic imprinted adsorbent for the treatment of copper-containing wastewater, which is prepared by the following method: dissolving soluble copper salt and acetic acid in chitosan solution, and the concentration of copper ions, chitosan and acetic acid The mass ratio is 1:(1~5):(1~4), heated and stirred to obtain the dispersed phase; then the continuous phase is cut into the dispersed phase with a microfluidic device, and the formed micro-droplets are introduced into the solidified liquid Cross-linking and curing; finally, the cured micro-droplets are desorbed with a desorbent, washed and dried to obtain the required adsorbent. The invention is simple in operation and low in cost, and the obtained adsorbent has specific selective adsorption performance for copper ions, fast adsorption speed, high adsorption capacity, and can be reused; using microfluidic granulation technology, the particle size is uniform and the composition , uniform in shape and size, and has far-reaching research prospects for the treatment of industrial wastewater containing copper ions.
Description
技术领域technical field
本发明涉及一种用于含铜废水处理的微流控合成印迹吸附剂,属于高分子复合材料技术领域。The invention relates to a microfluidic synthetic imprinted adsorbent for treating copper-containing wastewater, which belongs to the technical field of polymer composite materials.
背景技术Background technique
近年来,随着现代化工业的发展,废水中重金属污染已成为当前最严峻的环境问题之一。含重金属的废水可直接或间接的造成人类和牲畜的永久性中毒,铜对人体造血、细胞生长、人体某些酶的活动以及内分泌腺功能均有影响,如摄入过量的铜,就会刺激消化系统,引起腹痛、呕吐,甚至死亡。吸附技术在水污染控制和水净化领域发挥着其它技术无法替代的作用。吸附材料是指具有某种特定分子或离子,从而具有选择性亲和作用的高分子材料,这类材料一般具有较大的孔径和比表面积,能有效的从气体或液体中吸附其中某些成分的固体物质,具有制造方便、容易再生、较高的机械强度等特点。但传统的吸附材料由于很难生物降解,使用废弃后往往对环境造成污染。天然高分子化合物如纤维素、壳聚糖等具有多种功能基团,且来源经济广泛,具有良好的生物相容性和生物降解性能,因此,已成为制备吸附树脂的重要原料。In recent years, with the development of modern industry, heavy metal pollution in wastewater has become one of the most serious environmental problems. Wastewater containing heavy metals can directly or indirectly cause permanent poisoning of humans and livestock. Copper can affect human hematopoiesis, cell growth, activities of certain human enzymes, and endocrine gland functions. Excessive intake of copper will stimulate Digestive system, causing abdominal pain, vomiting, and even death. Adsorption technology plays an irreplaceable role in the field of water pollution control and water purification. Adsorption material refers to a polymer material that has a specific molecule or ion and thus has a selective affinity. This type of material generally has a large pore size and specific surface area, and can effectively adsorb some components from gases or liquids. It is a solid substance with the characteristics of convenient manufacture, easy regeneration, and high mechanical strength. However, traditional adsorption materials are difficult to biodegrade, and often cause environmental pollution after use and disposal. Natural polymers such as cellulose and chitosan have a variety of functional groups, are economically available, and have good biocompatibility and biodegradability. Therefore, they have become important raw materials for the preparation of adsorption resins.
传统的制备壳聚糖微球的方法有乳化‐交联法、反向悬浮法、单凝聚法等,这些方法大多存在微球尺寸不均一、不可控、制备效率不高、重复性较差等特点,而壳聚糖微球的大小和单分散性对于其吸附方面的应用至关重要。因此,应用微流控设备实现对微球的数目及大小的精确控制,制备出粒径均匀、高单分散性的吸附剂,实现了高效的吸附性能。为了能进一步的提高吸附过程的效率和可靠性,也是工业上对铜离子高效特定选择性吸附性能的需求,我们采用了离子印迹技术。The traditional methods for preparing chitosan microspheres include emulsification‐crosslinking method, reverse suspension method, single coacervation method, etc. Most of these methods have microsphere size inhomogeneity, uncontrollable, low preparation efficiency, poor repeatability, etc. characteristics, while the size and monodispersity of chitosan microspheres are critical for its adsorption applications. Therefore, the application of microfluidic equipment to achieve precise control of the number and size of microspheres, to prepare adsorbents with uniform particle size and high monodispersity, and to achieve efficient adsorption performance. In order to further improve the efficiency and reliability of the adsorption process, which is also the industrial demand for efficient and specific selective adsorption of copper ions, we have adopted ion imprinting technology.
离子印迹技术是指为获得在空间和结合位点上与某一离子完全匹配的聚合物的制备技术,这种聚合物被称为离子印迹聚合物。离子印迹聚合物带有许多固定形状和大小的空穴,空穴内通常带有确定排列的功能基团,它对印迹离子的立体结构具有记忆功能。Ion imprinting technology refers to the preparation technology to obtain a polymer that completely matches an ion in space and binding sites, and this polymer is called an ion imprinted polymer. Ion-imprinted polymers have many cavities with fixed shapes and sizes, and the cavities usually have functional groups in a definite arrangement, which have a memory function for the three-dimensional structure of imprinted ions.
因此,我们利用微流控及离子印迹技术制备的这种壳聚糖吸附剂对铜离子具有选择吸附性,吸附效率高,吸附溶液大,而且操作简单、成本低廉。Therefore, the chitosan adsorbent prepared by microfluidic and ion imprinting technology has selective adsorption for copper ions, high adsorption efficiency, large adsorption solution, simple operation and low cost.
发明内容Contents of the invention
为了提高对含铜离子工业废水的吸附效率以及满足对铜离子的特定选择吸附的需求,本发明出一种用于含铜废水处理的微流控合成印迹吸附剂,制作该吸附剂的方法操作简单,得到的吸附剂吸附效率高且对铜离子具有选择吸附性。In order to improve the adsorption efficiency of industrial wastewater containing copper ions and meet the demand for specific selective adsorption of copper ions, the present invention develops a microfluidic synthetic imprinted adsorbent for copper-containing wastewater treatment, and the method for making the adsorbent is operated The method is simple, and the obtained adsorbent has high adsorption efficiency and selective adsorption for copper ions.
本发明指通过如下技术方案实现的:The present invention refers to realize by following technical scheme:
一种用于含铜废水处理的微流控合成印迹吸附剂,其特征在于,所述的吸附剂是通过以下方法制备而成的:A microfluidic synthetic imprinted adsorbent for copper-containing wastewater treatment, characterized in that the adsorbent is prepared by the following method:
1)将可溶性的铜盐和乙酸溶解在壳聚糖溶液中,并加热搅拌,得到分散相,铜离子、壳聚糖和乙酸的质量比为1∶(1~5)∶(1~4),1) Dissolve soluble copper salt and acetic acid in chitosan solution, and heat and stir to obtain dispersed phase, the mass ratio of copper ion, chitosan and acetic acid is 1: (1~5): (1~4) ,
2)通过微流控装置用连续相剪切步骤1)所得的分散相,并将形成的微液滴引入到装有固化液的烧杯中进行交联固化,2) Shearing the dispersed phase obtained in step 1) with a continuous phase through a microfluidic device, and introducing the formed micro-droplets into a beaker containing a solidification solution for cross-linking and solidification,
3)将固化好的微液滴使用脱附剂进行脱附,并洗净、烘干,即制得用于含铜废水处理的微流控合成印迹吸附剂;3) Desorbing the solidified micro-droplets with a desorbent, washing and drying to obtain a microfluidic synthetic imprinted adsorbent for copper-containing wastewater treatment;
其中,连续相为司班与正辛烷或司班与正辛醇的混合溶液,司班在连续相中的质量分数为2%~4%,正辛烷或正辛醇为油相;Wherein, the continuous phase is a mixed solution of Span and n-octane or Span and n-octanol, the mass fraction of Span in the continuous phase is 2% to 4%, and n-octane or n-octanol is the oil phase;
固化液为连续相与固化剂的混合物,其中固化液中固化剂的质量分数为0.5%~2%,所述的固化剂为戊二醛、环氧氯丙烷、冠醚中的一种;The curing liquid is a mixture of a continuous phase and a curing agent, wherein the mass fraction of the curing agent in the curing liquid is 0.5% to 2%, and the curing agent is one of glutaraldehyde, epichlorohydrin, and crown ether;
可溶性铜盐可以为氯化铜、硫酸铜、硝酸铜、醋酸铜中的一种,这些铜盐提供的铜离子都为正二价的铜离子。The soluble copper salt can be one of copper chloride, copper sulfate, copper nitrate, and copper acetate, and the copper ions provided by these copper salts are all positive divalent copper ions.
所述步骤1)中,配制分散相的加热温度为50~80℃,时间为3~5小时。In the step 1), the heating temperature for preparing the dispersed phase is 50-80° C., and the heating time is 3-5 hours.
所述步骤2)中,使用微流控装置将连续相剪切分散相时,其分散相与连续相的流速比为(5:65)~(10:65)。In the step 2), when the continuous phase is sheared by the microfluidic device to the dispersed phase, the flow rate ratio of the dispersed phase to the continuous phase is (5:65)˜(10:65).
所述步骤2)中,烧杯中装有的固化液的量为40~80毫升,固化时间为0.5~3小时。In the step 2), the amount of solidified liquid contained in the beaker is 40-80 ml, and the solidified time is 0.5-3 hours.
所述步骤3)中,脱附剂可为硝酸、盐酸、乙二胺四乙酸中的一种,其浓度为0.1~0.5mol/L。In the step 3), the desorbing agent can be one of nitric acid, hydrochloric acid and ethylenediaminetetraacetic acid, and its concentration is 0.1-0.5mol/L.
所述步骤3)中,烘干温度为30~50℃,烘干时间为2~10小时。In the step 3), the drying temperature is 30-50° C., and the drying time is 2-10 hours.
本发明的优点:Advantages of the present invention:
本发明是基于微流控造粒技术应用离子印迹技术制备了一种用于含铜废水处理的微流控合成印迹吸附剂,该吸附剂对于铜离子具有选择吸附性,吸附效率高,吸附溶液大,操作简单、成本低廉,且具有可重复使用性能;使用微流控造粒技术,颗粒粒径均匀,组分、形貌和大小均一,对于含铜离子的工业废水的处理具有深远的研究前景。The present invention prepares a microfluidic synthetic imprinted adsorbent for the treatment of copper-containing wastewater based on the microfluidic granulation technology and the application of ion imprinting technology. The adsorbent has selective adsorption for copper ions and high adsorption efficiency. Large, simple operation, low cost, and reusable performance; using microfluidic granulation technology, the particle size is uniform, the composition, shape and size are uniform, and it has far-reaching research on the treatment of industrial wastewater containing copper ions prospect.
附图说明Description of drawings
图1为本发明制备的铜离子印迹吸附剂的制备过程示意图Fig. 1 is the schematic diagram of the preparation process of the copper ion imprinting adsorbent prepared by the present invention
具体实施方式detailed description
下面结合实施例对本发明作进一步阐述。The present invention will be further elaborated below in conjunction with embodiment.
实施例1:Example 1:
吸附剂的制备步骤:Sorbent preparation steps:
1)在100毫升的烧杯中加入1.6克壳聚糖,然后加入40毫升去离子水,再加入0.3824克的氯化铜晶体,放在磁力搅拌器上搅拌,搅拌的同时加入0.8毫升冰乙酸,充分溶解后,放在水浴锅中以60℃的恒温加热3小时,得到分散相;1) add 1.6 gram chitosan in the beaker of 100 milliliters, add 40 milliliters of deionized waters then, add the cupric chloride crystal of 0.3824 grams again, be placed on magnetic stirrer and stir, add 0.8 milliliters of glacial acetic acid while stirring, After fully dissolving, heat in a water bath at a constant temperature of 60°C for 3 hours to obtain a dispersed phase;
2)在250毫升烧杯中加入3克的司班,再加入209毫升的正辛烷,搅拌1小时得到连续相;在250毫升烧杯中加入3克的司班,再加入205毫升的正辛烷,最后加入3毫升的戊二醛,搅拌1小时得到水浴固化液;使用微流控装置,以分散相与连续相的流速比为5:65,用连续相剪切配制好的分散相,并将形成的液滴引入到装有60毫升水浴固化液的烧杯中,水浴固化1小时;2) Add 3 grams of Span in a 250 ml beaker, then add 209 ml of n-octane, stir for 1 hour to obtain a continuous phase; add 3 grams of Span in a 250 ml beaker, then add 205 ml of n-octane , finally add 3 ml of glutaraldehyde, stir for 1 hour to obtain a water bath solidification solution; use a microfluidic device, with the flow rate ratio of the dispersed phase and the continuous phase being 5:65, shear the prepared dispersed phase with the continuous phase, and The formed droplet is introduced into a beaker containing 60 milliliters of water-bath curing solution, and the water-bath is solidified for 1 hour;
3)将固化好的微液滴用乙醇溶液以及去离子水清洗,由于加入了离子印迹所需的铜盐,清洗完的微球呈淡绿色,然后使用乙二胺四乙酸脱附剂进行脱附15分钟,再次清洗抽滤,脱附后的微球则成淡黄色,可以很明显的看出颜色由淡绿色变成淡黄色,这说明之前配制分散相加入的印迹铜3) Wash the cured micro-droplets with ethanol solution and deionized water. Due to the addition of the copper salt required for ion imprinting, the cleaned microspheres are light green, and then use ethylenediaminetetraacetic acid desorbent for desorption. Attach for 15 minutes, wash and filter again, the desorbed microspheres turn light yellow, and it can be clearly seen that the color changes from light green to light yellow, which shows that the imprinted copper added to the previously prepared dispersed phase
盐已经被成功脱附下来,最后在40℃下烘干3小时,得到所需的吸附剂。The salt has been successfully desorbed, and finally dried at 40°C for 3 hours to obtain the desired adsorbent.
其整个制备流程如附图1所示,首先是壳聚糖与铜离子的螯合反应,其次是戊二醛的交联反应,最后是吸附剂的脱附过程。Its whole preparation process is shown in accompanying drawing 1, firstly is the chelation reaction of chitosan and copper ion, secondly is the cross-linking reaction of glutaraldehyde, finally is the desorption process of adsorbent.
实施例1制备的吸附剂对铜离子的吸附能力显著,吸附平衡时间为76小时,最大吸附量为75mg/g。The adsorbent prepared in Example 1 has remarkable adsorption capacity for copper ions, the adsorption equilibrium time is 76 hours, and the maximum adsorption capacity is 75 mg/g.
实施例2:Example 2:
按照实施例1的制备方法,把水浴固化时间改为3小时,制得所需的吸附剂,吸附铜离子后,得到其吸附平衡时间为85小时,最大吸附量为60mg/g。According to the preparation method of Example 1, the water bath solidification time was changed to 3 hours to obtain the required adsorbent. After absorbing copper ions, the adsorption equilibrium time was 85 hours and the maximum adsorption capacity was 60 mg/g.
实施例3:Example 3:
按照实施例1的制备方法,把加入氯化铜晶体的量改为0.1克,制得所需的吸附剂,吸附铜离子后,得到其吸附平衡时间为90小时,最大吸附量为68mg/g。According to the preparation method of Example 1, the amount of copper chloride crystals added was changed to 0.1 g to obtain the required adsorbent. After absorbing copper ions, the adsorption equilibrium time was 90 hours, and the maximum adsorption capacity was 68 mg/g. .
Claims (6)
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710128769.5A CN106861663A (en) | 2017-03-06 | 2017-03-06 | A kind of micro-fluidic synthesis trace adsorbent for copper-containing wastewater treatment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710128769.5A CN106861663A (en) | 2017-03-06 | 2017-03-06 | A kind of micro-fluidic synthesis trace adsorbent for copper-containing wastewater treatment |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN106861663A true CN106861663A (en) | 2017-06-20 |
Family
ID=59170605
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201710128769.5A Pending CN106861663A (en) | 2017-03-06 | 2017-03-06 | A kind of micro-fluidic synthesis trace adsorbent for copper-containing wastewater treatment |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN106861663A (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110314662A (en) * | 2019-08-02 | 2019-10-11 | 铁岭选矿药剂有限公司 | A kind of adsorbable Cu2+The preparation method of the novel membrane adsorbent of ion |
| CN110961084A (en) * | 2019-12-05 | 2020-04-07 | 常州大学 | A kind of preparation method of modified chitosan aerogel and its application to the adsorption of lithium ions |
Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102827380A (en) * | 2012-09-04 | 2012-12-19 | 清华大学 | Preparation method for metal ion printing chitosan porous micro-spheres |
| CN104741089A (en) * | 2015-02-15 | 2015-07-01 | 华东理工大学 | Method for preparing crosslinked-chitosan-system azo dye wastewater adsorbent |
-
2017
- 2017-03-06 CN CN201710128769.5A patent/CN106861663A/en active Pending
Patent Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102827380A (en) * | 2012-09-04 | 2012-12-19 | 清华大学 | Preparation method for metal ion printing chitosan porous micro-spheres |
| CN104741089A (en) * | 2015-02-15 | 2015-07-01 | 华东理工大学 | Method for preparing crosslinked-chitosan-system azo dye wastewater adsorbent |
Non-Patent Citations (1)
| Title |
|---|
| YONG ZHU ET AL.: "A facile ion imprinted synthesis of selective biosorbent for Cu2+ via microfluidic technology", 《JOURNAL OF CHEMICAL TECHNOLOGY & BIOTECHNOLOGY》 * |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110314662A (en) * | 2019-08-02 | 2019-10-11 | 铁岭选矿药剂有限公司 | A kind of adsorbable Cu2+The preparation method of the novel membrane adsorbent of ion |
| CN110961084A (en) * | 2019-12-05 | 2020-04-07 | 常州大学 | A kind of preparation method of modified chitosan aerogel and its application to the adsorption of lithium ions |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN103285837B (en) | Preparation method of adsorption material with high selectivity on different heavy metal ions | |
| CN101250267B (en) | Preparation method of cellulose microsphere | |
| CN102389780B (en) | A kind of water treatment agent and preparation method thereof | |
| CN109266851B (en) | Method for extracting lithium through magnetic microporous lithium adsorbent | |
| CN103127914B (en) | Magnetic chitosan microsphere treatment agent and preparation method thereof | |
| CN106179249B (en) | A kind of preparation method of concave convex rod cellulose composite adsorption microballoon | |
| CN101357325A (en) | A kind of spherical cellulose chelating adsorbent containing amidoxime group and carboxyl group and preparation method thereof | |
| CN107081138A (en) | Magnetic polystyrene base enclosure glycan composite adsorbent and preparation method and application | |
| CN103894159A (en) | Dye adsorbent capable of effectively removing anions from wastewater and preparation method of dye adsorbent | |
| CN108970589B (en) | Hydrotalcite-based composite gel ball and preparation method and application thereof | |
| CN105727907A (en) | Magnetic persimmon tannin composite adsorption material and preparing method thereof | |
| Liu et al. | Tentacle-type poly (hydroxamic acid)-modified macroporous cellulose beads: Synthesis, characterization, and application for heavy metal ions adsorption | |
| CN108816204A (en) | A kind of preparation method of copper ion imprinted crosslinked chitosan microballoon | |
| CN103007881A (en) | Magnetically separated bamboo charcoal-based wastewater treatment agent and preparation method and application thereof | |
| CN105921763B (en) | The preparation method of sodium alginate/inorganic mineral combined loading type nano zero valence iron | |
| CN107469769A (en) | A kind of preparation method and applications of magnetic adsorptive material | |
| CN105148855A (en) | Magnetic chitosan bamboo charcoal composite material, preparation method and application thereof | |
| CN106861663A (en) | A kind of micro-fluidic synthesis trace adsorbent for copper-containing wastewater treatment | |
| CN104549172B (en) | Method for preparing sulfydryl-modified chitosan short hole microspheres | |
| CN102580687A (en) | Polyamine-modified chitosan base expanded bed adsorbing medium and preparation method thereof | |
| CN110201648A (en) | A kind of diatomite surface A s(V) ion blotting adsorbent material preparation method | |
| CN107684903A (en) | A kind of method and Modified Quartz Sand for preparing the humic acid modified quartz sand of magnetic | |
| CN113351187B (en) | A kind of heavy metal ion imprinted hydrogel beads and preparation method and application thereof | |
| CN104741098B (en) | A kind of preparation method for being used to remove the resin material of copper ion in water | |
| CN103127917A (en) | Preparation method of drinking water treatment agent |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| PB01 | Publication | ||
| PB01 | Publication | ||
| SE01 | Entry into force of request for substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| WD01 | Invention patent application deemed withdrawn after publication | ||
| WD01 | Invention patent application deemed withdrawn after publication |
Application publication date: 20170620 |