CN106268666A - A kind of adsorbent - Google Patents
A kind of adsorbent Download PDFInfo
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- CN106268666A CN106268666A CN201610773445.2A CN201610773445A CN106268666A CN 106268666 A CN106268666 A CN 106268666A CN 201610773445 A CN201610773445 A CN 201610773445A CN 106268666 A CN106268666 A CN 106268666A
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- adsorbent
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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
- B01J20/22—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
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- 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
- C02F1/286—Treatment of water, waste water, or sewage by sorption using natural organic sorbents or derivatives thereof
-
- 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
- B01J2220/48—Sorbents characterised by the starting material used for their preparation
- B01J2220/4812—Sorbents characterised by the starting material used for their preparation the starting material being of organic character
- B01J2220/4825—Polysaccharides or cellulose materials, e.g. starch, chitin, sawdust, wood, straw, cotton
-
- 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
- B01J2220/48—Sorbents characterised by the starting material used for their preparation
- B01J2220/4812—Sorbents characterised by the starting material used for their preparation the starting material being of organic character
- B01J2220/485—Plants or land vegetals, e.g. cereals, wheat, corn, rice, sphagnum, peat moss
-
- 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
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- Chemical & Material Sciences (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)
- Analytical Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Abstract
The invention discloses a kind of Matteuccia strthiopteris modified adsorbent and preparation method thereof.Using Matteuccia strthiopteris as raw material, processing reaction process by isopropanol, potassium hydroxide solution and citric acid solution, modification is prepared as a kind of biomass adsorbent.The method abundant raw material source, with low cost and environmentally friendly, there is preferable application prospect.
Description
Technical field
The present invention relates to a kind of adsorbent, particularly to one using Matteuccia strthiopteris plant as raw material, the one of modified preparation
Adsorbent and technique, belong to sorbent material field.
Background technology
Along with the development of process of industrialization, heavy metal pollution is increasingly severe, owing to heavy metal can not be by microorganism
Degraded, can only occur the mutual conversion between various form in the environment, so, the elimination of heavy metal pollution is the most tired
Difficulty, can be enriched with in the body that heavy metal is lived, and causes various disease and body disorderly, very harmful to organism.
The technique that efficiently separates being presently used for removing heavy metal ions in sewage has: at the exchange of precipitation, ion, electrochemistry
Reason, membrane technology, evaporation coagulation, reverse osmosis and electrodialysis etc., but the application of these technology is limited, closely by technique and economy sometimes
Over Nian, organism absorption by living is removed the method for heavy metal and has been caused concern, this method mainly utilize hyperaccumulative plant,
Algae and microorganism heavy metal have bigger absorbability to remove the heavy metal in waste water, but process dirt with the organism lived
Water is limited by Biomass and the growth characteristics of organism itself, and such method is also unsuitable for applying on a large scale the most so far.
Modified cellulose class adsorbent is one of important development direction of current cellulose functional high molecule material.Such adsorbent does not draws
Entering new pollutant, consume energy low, so there being important application in water processes, and being more easy to regeneration than adsorbent resin again, and
Stability is high, and adsorptive selectivity is special, and adsorbent price is far below adsorbent resin.
Matteuccia strthiopteris widely distributed China various places, it contains a large amount of cellulose, can prepare cellulose modified adsorbent.This
Bright using Matteuccia strthiopteris as raw material, under the effect of isopropanol, potassium hydroxide solution and citric acid solution, modification is prepared as a kind of raw
Substance adsorber.
Summary of the invention
The present invention is to provide a kind of Matteuccia strthiopteris modified adsorbent and preparation method thereof.This preparation method passes through techniques below road
Line realizes:
By Matteuccia strthiopteris with clean water clean after, put into and baking oven carried out dry to constant weight;
(2) dried object pulverizer is pulverized, sieve;
(3) collect powder, by the isopropanol hybrid reaction of powder Yu certain solubility, and be stirred continuously;
(4) after reacting, solution filters, and is carried out with distilled water, and wash products is placed in drying baker and dries;
(5) the potassium hydroxide solution drying product and certain solubility reacts, and is stirred continuously and makes it react abundant;
(6) after reacting, solution filters, and is carried out with distilled water, and wash products is placed in drying baker and dries;
(7) the citric acid solution drying product and certain solubility reacts, and is stirred continuously and makes it fully react;
It is neutral that the most last distilled water is washed till solution, and filters, after drying product.
Preferentially, step (1) in, dry temperature be 50-70 DEG C.
Preferentially, step (2) in, the mesh number of sieve is 100-200 mesh.
Preferentially, step (3) in, the solubility of isopropanol is 15-20%, and the response time is 12-15 hour.
Preferentially, step (4), (6), (8) in, dry temperature conditions be at 50-60 DEG C, drying time is 10-20 hour.
Preferentially, step (5) in, the solubility of potassium hydroxide is 0.1-0.5mol/L, and the response time is 1-2 hour.
Preferentially, step (7) in, the solubility of citric acid is 0.5-1mol/L, and the response time is 2-4 hour.
The present invention has following advantages and a characteristic:
(1) abundant raw material source, with low cost;
(2) technique is simple, easily operates;
The most environmentally friendly, not secondary pollution.
Detailed description of the invention
Embodiment one:
By Matteuccia strthiopteris with clean water clean after, be then placed in the baking oven under the conditions of 50 DEG C carrying out drying to constant weight, then will be dry
Dry thing pulverizer is pulverized, and crosses 200 mesh sieves, weighs 10g powder and put in a container, then is 15% different toward pouring solubility in container into
Propanol, and be stirred continuously and make it fully react, after 12 hours, solution being filtered, and be carried out with distilled water, wash products is put
Drying in drying baker under the conditions of 50 DEG C, after drying 20 hours, drying object is reentered in container, then pours into
The potassium hydroxide solution of 0.1mol/L, and be stirred continuously and make it fully react, after 2 hours, solution is filtered, and enter with distilled water
Row cleans, and wash products is placed in the drying baker under the conditions of 50 DEG C and dries, and after drying 20 hours, dries product and is reentered into
In container, then pouring the citric acid solution of 0.5mol/L into, solution was filtered after 4 hours by stirring reaction, and carried out clearly with distilled water
Be washed till solution for neutrality, be finally placed in the drying baker under the conditions of 50 DEG C and dry, after drying 20 hours product.
Embodiment two:
By Matteuccia strthiopteris with clean water clean after, be then placed in the baking oven under the conditions of 60 DEG C carrying out drying to constant weight, then will be dry
Dry thing pulverizer is pulverized, and crosses 100 mesh sieves, weighs 20g powder and put in a container, then is 18% different toward pouring solubility in container into
Propanol, and be stirred continuously and make it fully react, after 13 hours, solution being filtered, and be carried out with distilled water, wash products is put
Drying in drying baker under the conditions of 55 DEG C, after drying 15 hours, drying object is reentered in container, then pours into
The potassium hydroxide solution of 0.5mol/L, and be stirred continuously and make it fully react, after 1 hour, solution is filtered, and enter with distilled water
Row cleans, and wash products is placed in the drying baker under the conditions of 55 DEG C and dries, and after drying 15 hours, dries product and is reentered into
In container, then pouring the citric acid solution of 1mol/L into, solution was filtered after 2 hours by stirring reaction, and was carried out with distilled water
Be neutral to solution, be finally placed in the drying baker under the conditions of 55 DEG C and dry, after drying 15 hours product.
Embodiment three:
By Matteuccia strthiopteris with clean water clean after, be then placed in the baking oven under the conditions of 70 DEG C carrying out drying to constant weight, then will be dry
Dry thing pulverizer is pulverized, and crosses 100 mesh sieves, weighs 20g powder and put in a container, then is 20% different toward pouring solubility in container into
Propanol, and be stirred continuously and make it fully react, after 15 hours, solution being filtered, and be carried out with distilled water, wash products is put
Drying in drying baker under the conditions of 60 DEG C, after drying 10 hours, drying object is reentered in container, then pours into
The potassium hydroxide solution of 0.5mol/L, and be stirred continuously and make it fully react, after 1 hour, solution is filtered, and enter with distilled water
Row cleans, and wash products is placed in the drying baker under the conditions of 60 DEG C and dries, and after drying 10 hours, dries product and is reentered into
In container, then pouring the citric acid solution of 1mol/L into, solution was filtered after 2 hours by stirring reaction, and was carried out with distilled water
Be neutral to solution, be finally placed in the drying baker under the conditions of 60 DEG C and dry, after drying 10 hours product.
Claims (7)
1. an adsorbent, it is characterised in that the preparation method of this adsorbent comprises the steps:
By Matteuccia strthiopteris with clean water clean after, put into and baking oven carried out dry to constant weight;
(2) dried object pulverizer is pulverized, sieve;
(3) collect powder, by the isopropanol hybrid reaction of powder Yu certain solubility, and be stirred continuously;
(4) after reacting, solution filters, and is carried out with distilled water, and wash products is placed in drying baker and dries;
(5) the potassium hydroxide solution drying product and certain solubility reacts, and is stirred continuously and makes it react abundant;
(6) after reacting, solution filters, and is carried out with distilled water, and wash products is placed in drying baker and dries;
(7) the citric acid solution drying product and certain solubility reacts, and is stirred continuously and makes it fully react;
It is neutral that the most last distilled water is washed till solution, and filters, after drying product.
A kind of adsorbent the most according to claim 1, it is characterised in that step (1) in, dry temperature and be 50-70 DEG C.
A kind of adsorbent the most according to claim 1, it is characterised in that step (2) in, the mesh number of sieve is 100-200 mesh.
A kind of adsorbent the most according to claim 1, it is characterised in that step (3) in, the solubility of isopropanol is 15-20%,
Response time is 12-15 hour.
A kind of adsorbent the most according to claim 1, it is characterised in that step (4), (6), (8) in, drying temperature conditions is
At 50-60 DEG C, drying time is 10-20 hour.
A kind of adsorbent the most according to claim 1, it is characterised in that step (5) in, the solubility of potassium hydroxide solution is
0.1-0.5mol/L, the response time is 1-2 hour.
A kind of adsorbent the most according to claim 1, it is characterised in that step (7) in, the solubility of citric acid is 0.5-
1mol/L, the response time is 2-4 hour.
Priority Applications (1)
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CN201610773445.2A CN106268666A (en) | 2016-08-31 | 2016-08-31 | A kind of adsorbent |
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CN201610773445.2A CN106268666A (en) | 2016-08-31 | 2016-08-31 | A kind of adsorbent |
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CN201610773445.2A Pending CN106268666A (en) | 2016-08-31 | 2016-08-31 | A kind of adsorbent |
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Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN115780499A (en) * | 2022-11-04 | 2023-03-14 | 四川农业大学 | Method for restoring manganese-polluted soil |
Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN105536715A (en) * | 2015-12-20 | 2016-05-04 | 吴涛 | Method for preparation of adsorption material by using maple leaf |
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2016
- 2016-08-31 CN CN201610773445.2A patent/CN106268666A/en active Pending
Patent Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN105536715A (en) * | 2015-12-20 | 2016-05-04 | 吴涛 | Method for preparation of adsorption material by using maple leaf |
Non-Patent Citations (1)
Title |
---|
王艳: "《蕨类植物》", 31 August 2014 * |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN115780499A (en) * | 2022-11-04 | 2023-03-14 | 四川农业大学 | Method for restoring manganese-polluted soil |
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