CN107297200A - A kind of foam coppe ferrite and its preparation and application using organic polyurethane foam as substrate - Google Patents
A kind of foam coppe ferrite and its preparation and application using organic polyurethane foam as substrate Download PDFInfo
- Publication number
- CN107297200A CN107297200A CN201710637482.5A CN201710637482A CN107297200A CN 107297200 A CN107297200 A CN 107297200A CN 201710637482 A CN201710637482 A CN 201710637482A CN 107297200 A CN107297200 A CN 107297200A
- Authority
- CN
- China
- Prior art keywords
- foam
- polyurethane foam
- coppe ferrite
- substrate
- arsenic
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Granted
Links
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
- B01J20/22—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
- B01J20/265—Synthetic macromolecular compounds modified or post-treated polymers
-
- 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
- B01J20/0203—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material comprising compounds of metals not provided for in B01J20/04
- B01J20/0225—Compounds of Fe, Ru, Os, Co, Rh, Ir, Ni, Pd, Pt
- B01J20/0229—Compounds of Fe
-
- 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
- B01J20/0203—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material comprising compounds of metals not provided for in B01J20/04
- B01J20/0233—Compounds of Cu, Ag, Au
- B01J20/0237—Compounds of Cu
-
- 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
- B01J20/28042—Shaped bodies; Monolithic structures
- B01J20/28045—Honeycomb or cellular structures; Solid foams or sponges
-
- 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
- C02F1/288—Treatment of water, waste water, or sewage by sorption using composite sorbents, e.g. coated, impregnated, multi-layered
-
- 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
- C02F1/48—Treatment of water, waste water, or sewage with magnetic or electric fields
- C02F1/488—Treatment of water, waste water, or sewage with magnetic or electric fields for separation of magnetic materials, e.g. magnetic flocculation
-
- 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
- C02F2101/103—Arsenic compounds
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2209/00—Controlling or monitoring parameters in water treatment
- C02F2209/06—Controlling or monitoring parameters in water treatment pH
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2303/00—Specific treatment goals
- C02F2303/16—Regeneration of sorbents, filters
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Analytical Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Life Sciences & Earth Sciences (AREA)
- Hydrology & Water Resources (AREA)
- Engineering & Computer Science (AREA)
- Environmental & Geological Engineering (AREA)
- Water Supply & Treatment (AREA)
- Inorganic Chemistry (AREA)
- Solid-Sorbent Or Filter-Aiding Compositions (AREA)
- Water Treatment By Sorption (AREA)
Abstract
The invention discloses a kind of foam coppe ferrite using organic polyurethane foam as substrate and its preparation and application.The foam coppe ferrite is that have coppe ferrite in organic polyurethane foam superficial growth.The invention provides application of the foam coppe ferrite in Adsorption arsenic in water body, the foam coppe ferrite not only has very strong adsorption capacity to the especially arsenic of the arsenic in water body (V), and because its substrate can be reclaimed easily, have and preferably recycle performance.
Description
(1) technical field
The present invention relates to a kind of foam coppe ferrite using organic polyurethane foam as substrate and preparation method thereof and the bubble
Application of the foam coppe ferrite in Adsorption arsenic in water body.
(2) background technology
Arsenic has Half-metallic, through improving alloy property frequently as alloy addition, for example, a small amount of arsenic is added in copper
Arsenical copper, which is made, can significantly reduce the thermal conductivity and electric conductivity of copper.It is applied in addition, arsenic is also often used as dopant material
Prepare some semi-conducting materials.The metallic compound of native arsenic or arsenic is extremely rare in nature, and they are mostly with sulfide
Form be mixed in other metallic ores, such as in copper, lead, zinc and cobalt ore.Exploitation and smelting with the mankind to arsenic-containing ores, with
And arsenide utilizes etc. the behavior directly or indirectly to affect arsenic migration in the environment and conversion process extensively.The opposing party
Face, arsenic and its compound are the carcinogenic substances that many authoritative institutions generally acknowledge in the world, and excess intake arsenic can cause very big danger to human body
Evil.After arsenic is absorbed by the body, trivalent arsenic may interfere with the reaction that internal phosphorus is participated in, and such as hinder the synthesis of atriphos, arsenic is also
It can be reacted with the sulfydryl of zymoprotein in body, enzyme is lost activity, cell eubolism is influenceed, so as to cause histologic lesion and machine
Body obstacle, directly results in poisoning even dead.Chronic Drinking water endemic arsenism can cause harm to human body multisystem function, cause as
The diseases such as hypertension, cardiovascular and cerebrovascular diseases, diabetes, skin pigment metabolic disorder, and finally develop into cutaneum carcinoma.In recent years, with
The quickening of process of industrialization, the arsenic pollution that industrial production is brought constantly expands, and the murder by poisoning of arsenic in water body at home and abroad has phase
Close report.
The international research mechanism such as World Health Organization unanimously assert that arsenic is that a kind of high poison element is also priority acccess control in water body
One of pollutant.The arsenic of different shape, toxicity is also different, and in general the toxicity of inorganic arsenic is bigger than organo-arsenic, trivalent arsenic
Toxicity it is bigger than pentavalent arsenic, and among the compound of arsenic, the toxicity of arsenic hydride is far longer than other arsenates and arsenite.
In worldwide, the acute or chronic arsenic poisoning because of caused by drinking water by arsenic pollution, and cause the diseases such as various cancers
Disease, or even dead case frequently occur, and these startling data have caused great attention of the people to Arsenic in Drinking Water.
1993, regulation arsenic content was limited to 10 μ g/L, world community in the new drinking water standard that the World Health Organization formulates
This standard is adopted one after another, and maximum allowable arsenic content standard in drinking water is brought up into 10 μ g/L from 50 original μ g/L.
The method of removing arsenic in water common at present has Coagulation Method, ion-exchange, absorption method, oxidation-precipitation method, bioanalysis
Etc..Absorption method is the prefered method of Removal of Arsenic in Drinking Water, the active aluminum oxide of common adsorbent, titanium oxide, zeolite, ferrimanganic
Compound etc., this method is easy to operate, and adsorbent is cheap, it is adaptable to factory's water body arsenic pollution processing.But powder is inhaled
Attached dose is difficult to reclaim and reuses, or even powder itself can produce secondary pollution to water body, thus is not suitable for lake, river
Arsenic pollution Deng water body in large is handled.
Therefore, a kind of new and effective repeatable adsorbent utilized is studied, the improvement for water body arsenic pollution has very
Important meaning.
(3) content of the invention
The purpose of the present invention is with organic foam for prior art to the deficiency of arsenic in water body pollution control there is provided one kind
Foam coppe ferrite for substrate and preparation method thereof and the application in Adsorption arsenic in water body, the foam coppe ferrite are not only right
Arsenic especially arsenic (V) in water body has very strong adsorption capacity, and because its substrate can be reclaimed easily, has preferably
Recycle performance.
For achieving the above object, the present invention is adopted the following technical scheme that:
It is in organic polyurethane foam the invention provides a kind of foam coppe ferrite using organic polyurethane foam as substrate
Superficial growth has coppe ferrite, and the foam coppe ferrite is prepared via a method which:
(1) polyurethane foam base is taken, the oil stain that immersion in NaOH solution removes surface is put into;Polyurethane after oil removing
Foam substrate is containing SnCl2Hydrochloric acid solution in carry out sensitized treatment, after taking-up wash drying;Then by the polyurethane after sensitization
Foam substrate is containing PdCl2Ethanol water in activated, after taking-up wash drying;
(2) it is 1 to weigh copper, iron mol ratio:1~1:5 ferric nitrate, copper nitrate are added in distilled water, after stirring and dissolving plus
Enter urea, the wherein mol ratio of nitrate and urea is 26:1-5:1, continue stir 10~60min, then with through step (1) place
The polyurethane foam base managed is put into reactor in the lump, and reactor is transferred in baking oven after sealing completely and be incubated instead
Should, reaction temperature is 50~200 DEG C, and soaking time is 3~12h;
(3) after the completion of reacting, the superficial growth polyurethane foam of coppe ferrite is taken out, distilled water cyclic washing is used, then
Dried in baking oven at 50~100 DEG C, obtain foam coppe ferrite.
In the present invention, foam coppe ferrite is black porous block foam-like after washing is dried, and surface main component is
CuFe2O4。
Further, in step (1), concentration of sodium hydroxide solution is preferably 1~3M.The preferred 2-10min of soak time.
Further, in step (1), the pore size of polyurethane foam base is 30ppi-120ppi.
Further, in step (1), containing SnCl2Hydrochloric acid solution in, SnCl2Concentration be 5-15g/L, hydrochloric acid mass concentration
For 0.5-3%.The sensitized treatment time is preferably 1-10min.
Further, in step (1), containing PdCl2Ethanol water in, PdCl2Concentration be 0.2-0.8 g/L, ethanol
With the volume ratio preferably 1 of water:1.Soak time is preferably 1-10min.
The invention provides a kind of preparation method of the foam coppe ferrite using organic polyurethane foam as substrate, according to as follows
Carry out:
(1) polyurethane foam base is taken, the oil stain that immersion in NaOH solution removes surface is put into;Polyurethane after oil removing
Foam substrate is containing SnCl2Hydrochloric acid solution in carry out sensitized treatment, after taking-up wash drying;Then by the polyurethane after sensitization
Foam substrate is containing PdCl2Ethanol water in activated, after taking-up wash drying;
(2) it is 1 to weigh copper, iron mol ratio:1~1:5 ferric nitrate, copper nitrate are added in distilled water, after stirring and dissolving plus
Enter urea, the wherein mol ratio of nitrate and urea is 26:1-5:1, continue stir 10~60min, then with through step (1) place
The polyurethane foam base managed is put into reactor in the lump, and reactor is transferred in baking oven after sealing completely and be incubated instead
Should, reaction temperature is 50~200 DEG C, and soaking time is 3~12h;
(3) after the completion of reacting, the superficial growth polyurethane foam of coppe ferrite is taken out, distilled water cyclic washing is used, then
Dried in baking oven at 50~100 DEG C, obtain foam coppe ferrite.
The preparation details of above-mentioned preparation method ibid, will not be repeated here.
Present invention also offers application of the foam coppe ferrite in Adsorption arsenic in water body, the application is specific
For:
(a) pH of arsenic-containing waste water is adjusted to 2~12, is put into foam coppe ferrite, with 100~400r/ at 10~60 DEG C
Min velocity fluctuation absorption;
(b) after vibration absorption, foam coppe ferrite, filtered wastewater, the water body after being handled are suctioned out with magnet.After absorption
Foam coppe ferrite can wash desorption with certain density NaOH solution, realize recycling.
Further, described arsenic is preferably As (V).
Further, As (V) content is 1~100mg/L in the arsenic-containing waste water.
Water body (i.e. arsenic-containing waste water) of the present invention is commercial metal Metallurgical Waste Water, surface water or sanitary sewage.
The beneficial effects of the invention are as follows:
(1) foam coppe ferrite of the present invention is compared to the nanoscale CuFe that existing literature is reported2O4, have for As (V)
There is higher adsorption capacity.
(2) preparation technology of foam coppe ferrite is simple and convenient to operate, efficiency high, is easily achieved, non-secondary pollution, economical
Environmental protection, realizes resource reproducible utilization, obtained
(3) present invention using foam ferrous acid polluted by copper arsenic removal method, adsorbent efficiently remove arsenic in water body while,
It can be separated easily using magnet with water body, and not produce secondary pollution, successfully solve existing arsenic in water body pollution control
Adsorbent difficulty recycles and reuses and easily causes the chronic illness of secondary pollution in journey.
(4) embodiment
The present invention is further detailed below by specific embodiment, but protection scope of the present invention and not only limited
In this.
Embodiment 1
It is 30ppi to take pore size, and size is 3cm × 3cm × 0.5cm polyurethane foam base, is put into 1MNaOH molten
The oil stain that 2min removes surface is soaked in liquid;Polyurethane foam after oil removing is in SnCl containing 10g/L2Mass percent be
Sensitized treatment 5min in 1.4% hydrochloric acid solution, washes drying after taking-up;Then by the polyurethane foam of sensitization containing 0.5g/L
PdCl2Ethanol water in (volume ratio of ethanol and water be 1:1) 3min is activated, drying is washed after taking-up.
It is 1 to weigh copper, iron mol ratio:1 nine water ferric nitrate 16.1g, nitrate trihydrate copper 9.6g pours into 100mL distilled water
Beaker in, stirring be completely dissolved after add 0.6g urea, continue stir 10min;With treated polyurethane after reaction completely
Foam substrate is put into reactor in the lump, and reactor is transferred in baking oven after sealing completely and is incubated, and reaction temperature is 50 DEG C,
Soaking time is 3h;After the completion of reaction, the superficial growth foamed iron of coppe ferrite is taken out, distilled water cyclic washing is used, then drying
Dried in case at 50 DEG C, obtain foam coppe ferrite.
The original solution containing arsenic that 50mL As (V) content is 10mg/L is taken in 250mL conical flasks, using hydrochloric acid by pH value of solution
3 are adjusted to, foam coppe ferrite made from one piece of addition is transferred to thermostatic control oscillator vibration, mixing speed is 200r/min, reaction temperature
Spend for 50 DEG C, adsorption time is 5-180min.
Adsorption effect of the foam coppe ferrite to arsenic in water body is assessed using adsorption rate.
The experimental result of the different adsorption times of table 1
Embodiment 2
It is 30ppi to take pore size, and size is 3cm × 3cm × 0.5cm polyurethane foam base, is put into 3MNaOH molten
The oil stain that 10min removes surface is soaked in liquid;Polyurethane foam after oil removing is in SnCl containing 10g/L2Mass percent be
Sensitized treatment 5min in 1.4% hydrochloric acid solution, washes drying after taking-up;Then by the polyurethane foam of sensitization containing 0.5g/L
PdCl2Ethanol water in (volume ratio of ethanol and water be 1:1) 3min is activated, drying is washed after taking-up.
It is 1 to weigh copper, iron mol ratio:5 nine water ferric nitrate 16.1g, nitrate trihydrate copper 48.0g pours into 100mL distilled water
Beaker in, stirring be completely dissolved after add 6g urea, continue stir 60min;With treated polyurethane foam after reaction completely
Foam substrate is put into reactor in the lump, and reactor is transferred in baking oven after sealing completely and is incubated, and reaction temperature is 200 DEG C,
Soaking time is 12h;After the completion of reaction, the superficial growth polyurethane foam base of coppe ferrite is taken out, is washed repeatedly with distilled water
Wash, then dry in an oven at 100 DEG C, obtain foam coppe ferrite.
The original solution containing arsenic that 50mL As (V) content is 10mg/L is taken in 250mL conical flasks, using hydrochloric acid by pH value of solution
3 are adjusted to, the foam coppe ferrite made from one piece is added, is transferred to thermostatic control oscillator vibration, mixing speed is 200r/min, is reacted
Temperature is 50 DEG C, and adsorption time is 5~180min.
Adsorption effect of the foam coppe ferrite to arsenic in water body is assessed using adsorption rate.
The experimental result of the different adsorption times of table 2
Embodiment 3
Foam ferrous acid copper Preparation Method be the same as Example 1.
Take 50mL As (V) content for 10mg/L original solutions containing arsenic in 250mL conical flasks, pH value of solution is adjusted using hydrochloric acid
To 3, foam coppe ferrite made from one piece of addition is transferred to thermostatic control oscillator vibration, mixing speed is 200r/min, reaction temperature
For 15~60 DEG C, adsorption time is 180min.
Adsorption effect of the foam coppe ferrite to arsenic in water body is assessed using adsorption rate.
The experimental result of the different adsorption temps of table 3
Temperature/DEG C | Adsorption rate/% of arsenic |
15 | 52.6 |
20 | 60.1 |
30 | 64.4 |
40 | 95.2 |
50 | 98.9 |
60 | 99.3 |
Embodiment 4
Foam ferrous acid copper Preparation Method be the same as Example 1.
Take 50mL As (V) content for 10mg/L original solutions containing arsenic in 250mL conical flasks, with salt acid for adjusting pH 2~12
It is 30ppi foam coppe ferrites to add pore size made from one piece, is transferred to thermostatic control oscillator vibration, mixing speed is 200r/
Min, reaction temperature is 50 DEG C, and adsorption time is 180min.
Displacement removal effect of the foam coppe ferrite to arsenic in water body is assessed using adsorption rate.
The difference of table 4 pH Adsorption experimental results
Embodiment 5
Foam ferrous acid copper Preparation Method be the same as Example 1.
50mL original solutions containing arsenic are taken in 250mL conical flasks, are adjusted pH in each conical flask to adding one after 3 with hydrochloric acid
Pore size made from block is 30ppi foam coppe ferrites, is transferred to thermostatic control oscillator vibration, mixing speed is 200r/min, instead
It is 50 DEG C to answer temperature, and adsorption time is 180min.
Displacement removal effect of the foam coppe ferrite to arsenic in water body is assessed using adsorption rate.
The Adsorption experimental results of the different arsenic concentrations of table 5
As (V) concentration/mgL-1 | Adsorption rate/% |
10 | 98.9 |
20 | 49.5 |
40 | 25.9 |
60 | 24.7 |
80 | 16.1 |
100 | 14.3 |
Embodiment 6
Foam ferrous acid copper Preparation Method be the same as Example 1, only changes the pore size of polyurethane foam base, obtains different holes
The foam coppe ferrite of footpath size.
Take 50mL As (V) content for 10mg/L original solutions containing arsenic in 250mL conical flasks, after salt acid for adjusting pH to 3
The foam coppe ferrite that one piece of different pore size size dimension is 3cm × 3cm × 0.5cm is separately added into, water bath with thermostatic control vibration is transferred to
Device, mixing speed is 200r/min, and reaction temperature is 50 DEG C, and adsorption time is 180 min.
Displacement removal effect of the foam coppe ferrite to arsenic in water body is assessed using adsorption rate.
The Adsorption experimental results of the different pore size size of table 6
Embodiment 7
Foam ferrous acid copper Preparation Method be the same as Example 1.
Prepare initial concentration be 5,10,20,40,60,80,100mg/L containing arsenic (V) original solution and adjusting pH=7, point
Do not take the above-mentioned original solutions containing arsenic of 50mL in 7 250mL conical flasks, be separately added into the sorbing material of one piece of phase homogenous quantities, shift
To thermostatic control oscillator vibration, mixing speed is 200r/min, and reaction temperature is 50 DEG C, and adsorption time is 180min.Compare 7 cones
Situation in shape bottle understands that the arsenic (V) of the sorbing material absorption of certain mass has a saturation value, after certain value,
Adsorbance is not further added by, and this is exactly saturated extent of adsorption, and the saturated extent of adsorption of unit mass is the adsorption capacity of sorbing material.Table
7 compare for the saturated capacity of three kinds of sorbing materials:
The adsorption capacity of table 7 compares
[a]:Y.-J.Tu,C.-F.You,C.-K.Chang,S.-L.Wang,T.-S.Chan,Adsorption
behavior of As(III)onto a copper ferrite generated from printed circuit board
industry,ChemEng J, 225(2013)433-439。
Claims (10)
1. a kind of foam coppe ferrite using organic polyurethane foam as substrate, is to have ferrous acid in organic polyurethane foam superficial growth
Copper, the foam coppe ferrite is prepared via a method which:
(1) polyurethane foam base is taken, the oil stain that immersion in NaOH solution removes surface is put into;Polyurethane foam after oil removing
Substrate is containing SnCl2Hydrochloric acid solution in carry out sensitized treatment, after taking-up wash drying;Then by the polyurethane foam after sensitization
Substrate is containing PdCl2Ethanol water in activated, after taking-up wash drying;
(2) it is 1 to weigh copper, iron mol ratio:1~1:5 ferric nitrate, copper nitrate are added in distilled water, and urine is added after stirring and dissolving
The mol ratio of element, wherein nitrate and urea is 26:1-5:1, continue to stir 10~60min, then with treating through step (1)
Polyurethane foam base be put into reactor in the lump, reactor is transferred in baking oven after sealing completely and carries out insulation reaction, instead
It is 50~200 DEG C to answer temperature, and soaking time is 3~12h;
(3) after the completion of reacting, the superficial growth polyurethane foam of coppe ferrite is taken out, distilled water cyclic washing is used, then in baking oven
In dry at 50~100 DEG C, obtain foam coppe ferrite.
2. the foam coppe ferrite as claimed in claim 1 by substrate of organic polyurethane foam, it is characterised in that:Step (1)
In, concentration of sodium hydroxide solution is 1~3M, and soak time is 2-10min.
3. the foam coppe ferrite as claimed in claim 1 by substrate of organic polyurethane foam, it is characterised in that:Step (1)
In, the pore size of polyurethane foam base is 30ppi-120ppi.
4. the foam coppe ferrite as claimed in claim 1 by substrate of organic polyurethane foam, it is characterised in that:Step (1)
In, containing SnCl2Hydrochloric acid solution in, SnCl2Concentration be 5-15g/L, hydrochloric acid mass concentration be 0.5-3%;The sensitized treatment time
For 1-10min.
5. the foam coppe ferrite as claimed in claim 1 by substrate of organic polyurethane foam, it is characterised in that:Step (1)
In, containing PdCl2Ethanol water in, PdCl2Concentration be 0.2-0.8g/L, the volume ratio of ethanol and water is 1:1;Activation
Time is 1-10min.
6. a kind of preparation method of the foam coppe ferrite as claimed in claim 1 by substrate of organic polyurethane foam, according to
It is carried out as follows:
(1) polyurethane foam base is taken, the oil stain that immersion in NaOH solution removes surface is put into;Polyurethane foam after oil removing
Substrate is containing SnCl2Hydrochloric acid solution in carry out sensitized treatment, after taking-up wash drying;Then by the polyurethane foam after sensitization
Substrate is containing PdCl2Ethanol water in activated, after taking-up wash drying;
(2) it is 1 to weigh copper, iron mol ratio:1~1:5 ferric nitrate, copper nitrate are added in distilled water, and urine is added after stirring and dissolving
The mol ratio of element, wherein nitrate and urea is 26:1-5:1, continue to stir 10~60min, then with treating through step (1)
Polyurethane foam base be put into reactor in the lump, reactor is transferred in baking oven after sealing completely and carries out insulation reaction, instead
It is 50~200 DEG C to answer temperature, and soaking time is 3~12h;
(3) after the completion of reacting, the superficial growth polyurethane foam of coppe ferrite is taken out, distilled water cyclic washing is used, then in baking oven
In dry at 50~100 DEG C, obtain foam coppe ferrite.
7. preparation method as claimed in claim 1, it is characterised in that:In step (1), the pore size of polyurethane foam base
For 30ppi-120ppi.
8. the foam coppe ferrite by substrate of organic polyurethane foam is in Adsorption arsenic in water body as claimed in claim 1
Application, the application is specially:
(a) pH of arsenic-containing waste water is adjusted to 2~12, is put into foam coppe ferrite, with 100~400r/min's at 10~60 DEG C
Velocity fluctuation is adsorbed;
(b) after vibration absorption, foam coppe ferrite, filtered wastewater, the water body after being handled are suctioned out with magnet.
9. application as claimed in claim 8, it is characterised in that:Described arsenic is As (V).
10. application as claimed in claim 9, it is characterised in that:As (V) content is 1~100mg/L in the arsenic-containing waste water.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201710637482.5A CN107297200B (en) | 2017-07-31 | 2017-07-31 | Foamed copper ferrite with organic polyurethane foam as substrate and preparation and application thereof |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201710637482.5A CN107297200B (en) | 2017-07-31 | 2017-07-31 | Foamed copper ferrite with organic polyurethane foam as substrate and preparation and application thereof |
Publications (2)
Publication Number | Publication Date |
---|---|
CN107297200A true CN107297200A (en) | 2017-10-27 |
CN107297200B CN107297200B (en) | 2020-06-23 |
Family
ID=60133368
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201710637482.5A Active CN107297200B (en) | 2017-07-31 | 2017-07-31 | Foamed copper ferrite with organic polyurethane foam as substrate and preparation and application thereof |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN107297200B (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN111019148A (en) * | 2019-12-10 | 2020-04-17 | 河南科技学院 | Modified foamed copper material and preparation method and application thereof |
CN113828281A (en) * | 2021-09-18 | 2021-12-24 | 集美大学 | Preparation method, product and application of polyurethane composite material |
CN114632499A (en) * | 2022-03-18 | 2022-06-17 | 中南大学 | Integrated molding material for emergency treatment of mercury-polluted water body and preparation method and application thereof |
Citations (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN1740216A (en) * | 2005-09-27 | 2006-03-01 | 北京理工大学 | Polyurethane foam metallizing treatment process |
CN1772382A (en) * | 2005-04-07 | 2006-05-17 | 上海亚兰德新能源材料有限公司 | Metal carrier for automobile tail gas purifier catalyst and its prepn |
CN102527387A (en) * | 2011-12-26 | 2012-07-04 | 南京理工大学 | Copper ferrite-graphene nano complex and preparation method thereof |
CN102949981A (en) * | 2011-08-17 | 2013-03-06 | 香港城市大学 | Porous substrate and one-dimensional nano-material composite material and its preparation method, and surface-modified composite material and its preparation method |
CN104087975A (en) * | 2013-12-19 | 2014-10-08 | 浙江工商大学 | Preparation method of foamed copper |
CN105749980A (en) * | 2016-02-04 | 2016-07-13 | 中国地质大学(北京) | Bismuth oxyhalogen photocatalytic foam and preparation method thereof |
-
2017
- 2017-07-31 CN CN201710637482.5A patent/CN107297200B/en active Active
Patent Citations (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN1772382A (en) * | 2005-04-07 | 2006-05-17 | 上海亚兰德新能源材料有限公司 | Metal carrier for automobile tail gas purifier catalyst and its prepn |
CN1740216A (en) * | 2005-09-27 | 2006-03-01 | 北京理工大学 | Polyurethane foam metallizing treatment process |
CN102949981A (en) * | 2011-08-17 | 2013-03-06 | 香港城市大学 | Porous substrate and one-dimensional nano-material composite material and its preparation method, and surface-modified composite material and its preparation method |
CN102527387A (en) * | 2011-12-26 | 2012-07-04 | 南京理工大学 | Copper ferrite-graphene nano complex and preparation method thereof |
CN104087975A (en) * | 2013-12-19 | 2014-10-08 | 浙江工商大学 | Preparation method of foamed copper |
CN105749980A (en) * | 2016-02-04 | 2016-07-13 | 中国地质大学(北京) | Bismuth oxyhalogen photocatalytic foam and preparation method thereof |
Non-Patent Citations (1)
Title |
---|
GAOSHENG ZHANG ET AL.: "Nanostructured iron(III)-copper(II) binary oxide: A novel adsorbent for enhanced arsenic removal from aqueous solutions", 《WATER RESEARCH》 * |
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN111019148A (en) * | 2019-12-10 | 2020-04-17 | 河南科技学院 | Modified foamed copper material and preparation method and application thereof |
CN111019148B (en) * | 2019-12-10 | 2021-10-01 | 河南科技学院 | Modified foamed copper material and preparation method and application thereof |
CN113828281A (en) * | 2021-09-18 | 2021-12-24 | 集美大学 | Preparation method, product and application of polyurethane composite material |
CN114632499A (en) * | 2022-03-18 | 2022-06-17 | 中南大学 | Integrated molding material for emergency treatment of mercury-polluted water body and preparation method and application thereof |
CN114632499B (en) * | 2022-03-18 | 2023-01-03 | 中南大学 | Integrated molding material for emergency treatment of mercury-polluted water body and preparation method and application thereof |
Also Published As
Publication number | Publication date |
---|---|
CN107297200B (en) | 2020-06-23 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN107297200A (en) | A kind of foam coppe ferrite and its preparation and application using organic polyurethane foam as substrate | |
CN106495377B (en) | A kind of processing method that nickel waste water is complexed | |
CN110302841A (en) | Preparation method of foamed nickel supported type bimetallic MOF base ozone catalyst and products thereof and application | |
CN104888748A (en) | Modified meerschaum, preparation method and application thereof | |
CN104258817B (en) | The chitosan magnetic of melamine modification, preparation method and applications | |
CN108002472A (en) | A kind of preparation method of domestic sewage treating compound | |
CN106861654A (en) | The immobilization particle and its preparation and application of a kind of same for treating acidic mine wastewater | |
CN108483582B (en) | Nitrite high-efficiency degradation material and preparation method and application thereof | |
CN104961199A (en) | Preparation method of Pd-Fe/foamed nickel three-dimensional particle electrodes | |
CN106582538A (en) | Preparation and regeneration method of EDTA-Na2 modified active carbon | |
Yu et al. | Facile fabrication of Cu (II) coordinated chitosan-based magnetic material for effective adsorption of reactive brilliant red from aqueous solution | |
CN110841714A (en) | Iron-cobalt bimetal-organic framework material based on 2, 5-dihydroxy terephthalic acid ligand and preparation method and application thereof | |
CN105668719A (en) | Cobalt oxide loaded active carbon catalytic particle electrode and preparation method thereof | |
CN108249523A (en) | Activated carbon catalysis granule electrode of supported ferriferous oxide and preparation method thereof | |
CN107362768A (en) | A kind of foam coppe ferrite and preparation method thereof and the application in Adsorption arsenic in water body | |
CN107442065A (en) | A kind of foam coppe ferrite/graphene oxide and its preparation and application | |
CN114835201A (en) | Three-dimensional electro-catalytic reaction equipment system based on multifunctional catalytic particle electrode | |
Liang et al. | Effective green treatment of sewage sludge from Fenton reactions: utilizing MoS2 for sustainable resource recovery | |
CN106732345A (en) | A kind of composite adsorbing material for heavy metal containing wastewater treatment and preparation method thereof | |
Wang et al. | Citric ligand manipulated efficient spatially-separated reduction and immobilization of Cr (VI) upon electron-rich copper-iron oxides | |
CN110404504B (en) | Cu-doped walnut shell activated carbon for treating printing and dyeing sewage and preparation method and application thereof | |
CN106552615A (en) | The preparation method of Concave-convex clay rod composite catalyzing material | |
CN107626325B (en) | Nickel-doped manganese ferrite-coated magnesium silicate composite catalyst and preparation method and application thereof | |
CN106215851A (en) | The preparation method and applications of the nano aluminium oxide that a kind of cupferron is modified | |
CN107413319A (en) | Method of the preparation of corncob modified magnetic heavy-metal adsorption material with removing heavy metal in water removal |
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 | ||
GR01 | Patent grant | ||
GR01 | Patent grant |