CN108927218A - A kind of polyaniline-coated biology carbon material and its preparing the application in solid base - Google Patents
A kind of polyaniline-coated biology carbon material and its preparing the application in solid base Download PDFInfo
- Publication number
- CN108927218A CN108927218A CN201810743453.1A CN201810743453A CN108927218A CN 108927218 A CN108927218 A CN 108927218A CN 201810743453 A CN201810743453 A CN 201810743453A CN 108927218 A CN108927218 A CN 108927218A
- Authority
- CN
- China
- Prior art keywords
- polyaniline
- carbon material
- coated
- hours
- coated biology
- 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
- 239000003575 carbonaceous material Substances 0.000 title claims abstract description 61
- 229920000767 polyaniline Polymers 0.000 title claims abstract description 42
- 239000007787 solid Substances 0.000 title abstract description 7
- PAYRUJLWNCNPSJ-UHFFFAOYSA-N Aniline Chemical compound NC1=CC=CC=C1 PAYRUJLWNCNPSJ-UHFFFAOYSA-N 0.000 claims abstract description 24
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 claims abstract description 24
- ROOXNKNUYICQNP-UHFFFAOYSA-N ammonium persulfate Chemical compound [NH4+].[NH4+].[O-]S(=O)(=O)OOS([O-])(=O)=O ROOXNKNUYICQNP-UHFFFAOYSA-N 0.000 claims abstract description 22
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 claims abstract description 12
- 229910001870 ammonium persulfate Inorganic materials 0.000 claims abstract description 11
- 238000002360 preparation method Methods 0.000 claims abstract description 11
- 238000005406 washing Methods 0.000 claims abstract description 11
- 238000001914 filtration Methods 0.000 claims abstract description 8
- 238000001035 drying Methods 0.000 claims abstract description 7
- 244000017020 Ipomoea batatas Species 0.000 claims abstract description 6
- 235000002678 Ipomoea batatas Nutrition 0.000 claims abstract description 6
- 238000003763 carbonization Methods 0.000 claims abstract description 6
- 229910052757 nitrogen Inorganic materials 0.000 claims abstract description 6
- 239000002244 precipitate Substances 0.000 claims abstract description 6
- 238000002604 ultrasonography Methods 0.000 claims abstract description 6
- 238000010792 warming Methods 0.000 claims abstract description 6
- 239000003513 alkali Substances 0.000 claims description 19
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 14
- 238000002156 mixing Methods 0.000 claims description 13
- BWHMMNNQKKPAPP-UHFFFAOYSA-L potassium carbonate Substances [K+].[K+].[O-]C([O-])=O BWHMMNNQKKPAPP-UHFFFAOYSA-L 0.000 claims description 13
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 claims description 10
- 238000000498 ball milling Methods 0.000 claims description 9
- 229960000935 dehydrated alcohol Drugs 0.000 claims description 9
- 229910000027 potassium carbonate Inorganic materials 0.000 claims description 8
- 239000002253 acid Substances 0.000 claims description 6
- 239000000463 material Substances 0.000 claims description 3
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 2
- QGZKDVFQNNGYKY-UHFFFAOYSA-O Ammonium Chemical compound [NH4+] QGZKDVFQNNGYKY-UHFFFAOYSA-O 0.000 claims 1
- 229910052799 carbon Inorganic materials 0.000 claims 1
- 239000011698 potassium fluoride Substances 0.000 claims 1
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 description 45
- 239000000047 product Substances 0.000 description 37
- PEDCQBHIVMGVHV-UHFFFAOYSA-N glycerol group Chemical group OCC(O)CO PEDCQBHIVMGVHV-UHFFFAOYSA-N 0.000 description 29
- 239000003225 biodiesel Substances 0.000 description 19
- 239000000243 solution Substances 0.000 description 18
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 14
- 238000006243 chemical reaction Methods 0.000 description 13
- 235000011187 glycerol Nutrition 0.000 description 12
- 239000007788 liquid Substances 0.000 description 11
- 238000003756 stirring Methods 0.000 description 10
- 239000003054 catalyst Substances 0.000 description 9
- 235000014113 dietary fatty acids Nutrition 0.000 description 9
- 239000000194 fatty acid Substances 0.000 description 9
- 229930195729 fatty acid Natural products 0.000 description 9
- 239000004519 grease Substances 0.000 description 8
- 238000004064 recycling Methods 0.000 description 8
- 239000006228 supernatant Substances 0.000 description 8
- 125000004836 hexamethylene group Chemical group [H]C([H])([*:2])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])[*:1] 0.000 description 7
- 238000013517 stratification Methods 0.000 description 7
- 238000005119 centrifugation Methods 0.000 description 6
- 239000003921 oil Substances 0.000 description 6
- 235000019198 oils Nutrition 0.000 description 6
- 235000011121 sodium hydroxide Nutrition 0.000 description 6
- PVNIQBQSYATKKL-UHFFFAOYSA-N tripalmitin Chemical compound CCCCCCCCCCCCCCCC(=O)OCC(OC(=O)CCCCCCCCCCCCCCC)COC(=O)CCCCCCCCCCCCCCC PVNIQBQSYATKKL-UHFFFAOYSA-N 0.000 description 6
- 239000007864 aqueous solution Substances 0.000 description 5
- 239000002585 base Substances 0.000 description 5
- 150000004665 fatty acids Chemical class 0.000 description 5
- 230000003197 catalytic effect Effects 0.000 description 4
- 238000001816 cooling Methods 0.000 description 4
- 239000007789 gas Substances 0.000 description 4
- 150000002632 lipids Chemical class 0.000 description 4
- 238000000034 method Methods 0.000 description 4
- 239000003549 soybean oil Substances 0.000 description 4
- 235000012424 soybean oil Nutrition 0.000 description 4
- -1 stratification Substances 0.000 description 4
- 150000002148 esters Chemical class 0.000 description 3
- 238000004519 manufacturing process Methods 0.000 description 3
- PHYFQTYBJUILEZ-IUPFWZBJSA-N triolein Chemical compound CCCCCCCC\C=C/CCCCCCCC(=O)OCC(OC(=O)CCCCCCC\C=C/CCCCCCCC)COC(=O)CCCCCCC\C=C/CCCCCCCC PHYFQTYBJUILEZ-IUPFWZBJSA-N 0.000 description 3
- 229960001947 tripalmitin Drugs 0.000 description 3
- 238000005292 vacuum distillation Methods 0.000 description 3
- QHZLMUACJMDIAE-UHFFFAOYSA-N 1-monopalmitoylglycerol Chemical compound CCCCCCCCCCCCCCCC(=O)OCC(O)CO QHZLMUACJMDIAE-UHFFFAOYSA-N 0.000 description 2
- 239000002283 diesel fuel Substances 0.000 description 2
- 239000003344 environmental pollutant Substances 0.000 description 2
- 231100000719 pollutant Toxicity 0.000 description 2
- 238000005809 transesterification reaction Methods 0.000 description 2
- 239000000263 2,3-dihydroxypropyl (Z)-octadec-9-enoate Substances 0.000 description 1
- RZRNAYUHWVFMIP-GDCKJWNLSA-N 3-oleoyl-sn-glycerol Chemical compound CCCCCCCC\C=C/CCCCCCCC(=O)OC[C@H](O)CO RZRNAYUHWVFMIP-GDCKJWNLSA-N 0.000 description 1
- 235000019482 Palm oil Nutrition 0.000 description 1
- 235000019483 Peanut oil Nutrition 0.000 description 1
- 235000019484 Rapeseed oil Nutrition 0.000 description 1
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 1
- 238000005815 base catalysis Methods 0.000 description 1
- 239000008162 cooking oil Substances 0.000 description 1
- 238000005260 corrosion Methods 0.000 description 1
- 230000007797 corrosion Effects 0.000 description 1
- 238000003912 environmental pollution Methods 0.000 description 1
- 239000003925 fat Substances 0.000 description 1
- 125000005313 fatty acid group Chemical group 0.000 description 1
- 235000019387 fatty acid methyl ester Nutrition 0.000 description 1
- 239000000446 fuel Substances 0.000 description 1
- 125000005456 glyceride group Chemical group 0.000 description 1
- 238000007172 homogeneous catalysis Methods 0.000 description 1
- 239000002815 homogeneous catalyst Substances 0.000 description 1
- 238000009776 industrial production Methods 0.000 description 1
- 239000010842 industrial wastewater Substances 0.000 description 1
- 229910052500 inorganic mineral Inorganic materials 0.000 description 1
- 150000004702 methyl esters Chemical class 0.000 description 1
- 239000011707 mineral Substances 0.000 description 1
- 235000010755 mineral Nutrition 0.000 description 1
- RZRNAYUHWVFMIP-UHFFFAOYSA-N monoelaidin Natural products CCCCCCCCC=CCCCCCCCC(=O)OCC(O)CO RZRNAYUHWVFMIP-UHFFFAOYSA-N 0.000 description 1
- 238000006386 neutralization reaction Methods 0.000 description 1
- 238000000696 nitrogen adsorption--desorption isotherm Methods 0.000 description 1
- ZQPPMHVWECSIRJ-KTKRTIGZSA-N oleic acid group Chemical group C(CCCCCCC\C=C/CCCCCCCC)(=O)O ZQPPMHVWECSIRJ-KTKRTIGZSA-N 0.000 description 1
- 239000002540 palm oil Substances 0.000 description 1
- 239000000312 peanut oil Substances 0.000 description 1
- 230000001376 precipitating effect Effects 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 238000001291 vacuum drying Methods 0.000 description 1
- 235000015112 vegetable and seed oil Nutrition 0.000 description 1
- 239000008158 vegetable oil Substances 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
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
- B01J31/00—Catalysts comprising hydrides, coordination complexes or organic compounds
- B01J31/02—Catalysts comprising hydrides, coordination complexes or organic compounds containing organic compounds or metal hydrides
- B01J31/06—Catalysts comprising hydrides, coordination complexes or organic compounds containing organic compounds or metal hydrides containing polymers
-
- B01J35/396—
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C67/00—Preparation of carboxylic acid esters
- C07C67/03—Preparation of carboxylic acid esters by reacting an ester group with a hydroxy group
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
- C10L1/00—Liquid carbonaceous fuels
- C10L1/02—Liquid carbonaceous fuels essentially based on components consisting of carbon, hydrogen, and oxygen only
-
- C—CHEMISTRY; METALLURGY
- C11—ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
- C11C—FATTY ACIDS FROM FATS, OILS OR WAXES; CANDLES; FATS, OILS OR FATTY ACIDS BY CHEMICAL MODIFICATION OF FATS, OILS, OR FATTY ACIDS OBTAINED THEREFROM
- C11C3/00—Fats, oils, or fatty acids by chemical modification of fats, oils, or fatty acids obtained therefrom
- C11C3/04—Fats, oils, or fatty acids by chemical modification of fats, oils, or fatty acids obtained therefrom by esterification of fats or fatty oils
- C11C3/10—Ester interchange
-
- 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
- B01J2231/00—Catalytic reactions performed with catalysts classified in B01J31/00
- B01J2231/40—Substitution reactions at carbon centres, e.g. C-C or C-X, i.e. carbon-hetero atom, cross-coupling, C-H activation or ring-opening reactions
- B01J2231/49—Esterification or transesterification
Abstract
The present invention relates to a kind of polyaniline-coated biology carbon material and its preparing the application in solid base; the preparation method of the polyaniline-coated biology carbon material includes the following steps: that (1) takes dry sweet potato leaves; under nitrogen protection; it is warming up to 600-700 degree; after carbonization 5-6 hours; cooled to room temperature obtains biological carbon material;(2) after the biological carbon material hydrochloric acid solution ultrasound for obtaining step (1) is impregnated 4-5 hours, aniline is added, under ice bath, ammonium persulfate solution is added, 6-10h is reacted in continuation under ice bath, and filtering, washing of precipitate are drying to obtain polyaniline-coated biology carbon material.
Description
Technical field
The invention belongs to biodiesel catalyst fields, and in particular to a kind of polyaniline-coated biology carbon material and its make
Application in standby solid base.
Background technique
Biodiesel becomes the hot spot of various countries' research because of its environment friendly, reproducibility.Biodiesel is with vegetable oil, dynamic
Object fat oil, waste cooking oils etc. are raw material, carry out transesterification with the alcohol of low molecular weight respectively and fatty acid alkyl monoesters are made,
Property is very close with mineral diesel, is a kind of reproducible clean fuel.Although the method for existing many preparation biodiesel,
But large-scale industrial production, it still uses based on the homogeneous catalysis such as traditional liquid acid, alkali, common homogeneous catalyst has
CaO、H2SO4, NaOH etc., severe corrosion to equipment, and product need to carry out neutralization washing, so as to cause a large amount of industrial wastewaters
It generates, causes environmental pollution.The present invention provides a kind of polyaniline-coated biology carbon material supported solid base catalyst, can be with
Efficiently preparation biodiesel, has the characteristics that reaction condition is mild, easily separated, reusable.
Summary of the invention
The present invention provides a kind of polyaniline-coated biology carbon material, it is characterised in that the polyaniline-coated biology carbon material
Preparation method include the following steps:
(1) dry sweet potato leaves are taken, under nitrogen protection, are warming up to 600-700 degree, after carbonization 5-6 hours, natural cooling
To room temperature, biological carbon material is obtained;
(2) after the biological carbon material hydrochloric acid solution ultrasound for obtaining step (1) is impregnated 4-5 hours, aniline, ice bath is added
Under, ammonium persulfate solution is added, 6-10h is reacted in continuation under ice bath, and filtering, washing of precipitate are drying to obtain polyaniline-coated life
Object carbon material.
The preferred 1.0-2.0mol/L of concentration of hydrochloric acid described in step (2), every gram of biological carbon materials'use 10-15mL hydrochloric acid
Solution, every gram of biological carbon materials'use aniline 0.5mL, every milliliter of aniline use 10-15mmol ammonium persulfate, the ammonium persulfate
The preferred 0.5-1.0mol/L of the concentration of solution;Supersonic frequency is 30-40kHz.
Another embodiment of the present invention provides application of the above-mentioned polyaniline-coated biology carbon material in load alkali.
Another embodiment of the present invention provides a kind of polyaniline-coated biology carbon material supported alkali, it is characterised in that described
The preparation method of the carbon material supported alkali of polyaniline-coated biology includes the following steps:
(1) dry sweet potato leaves are taken, under nitrogen protection, are warming up to 600-700 degree, after carbonization 5-6 hours, natural cooling
To room temperature, biological carbon material is obtained;
(2) after the biological carbon material hydrochloric acid solution ultrasound for obtaining step (1) is impregnated 4-5 hours, aniline, ice bath is added
Under, ammonium persulfate solution is added, 6-10h is reacted in continuation under ice bath, and filtering, washing of precipitate are drying to obtain polyaniline-coated life
Object carbon material.
(3) the polyaniline-coated biology carbon material for obtaining step (2) and KF, K2CO3After mixing and ball milling 6 hours, successively use
Water, dehydrated alcohol washing, be dried in vacuo under the conditions of 90 DEG C be dried in vacuo for 24 hours up to polyaniline-coated biology it is carbon material supported
Alkali.
The preferred 1.0-2.0mol/L of concentration of hydrochloric acid described in step (2), every gram of biological carbon materials'use 10-15mL hydrochloric acid
Solution, every gram of biological carbon materials'use aniline 0.5mL, every milliliter of aniline use 10-15mmol ammonium persulfate, the ammonium persulfate
The preferred 0.5-1.0mol/L of the concentration of solution;Supersonic frequency is 30-40kHz.
Polyaniline-coated biology carbon material, KF, K in step (3)2CO3Mass ratio be 1:1:3.
It is anti-in catalytic transesterification that another embodiment of the present invention provides the carbon material supported alkali of above-mentioned polyaniline-coated biology
Application in answering.
Another embodiment of the present invention provides the carbon material supported alkali of above-mentioned polyaniline-coated biology in preparation biodiesel
In application.
Another embodiment of the present invention provides a kind of preparation method of biodiesel, it is characterised in that including walking as follows
It is rapid:
(1) the deacidification processing of grease: suitable sodium hydrate aqueous solution is added into grease, after stirring 0.5-1.0h, turns
Enter in separatory funnel, stratification, collect supernatant liquid, after 50-60 DEG C of water washing to neutrality, be added hexamethylene, with point
Hydrophone removes extra moisture, and finally vacuum distillation removes hexamethylene to get acid lipid is removed;
(2) after acid lipid, methanol, catalyst mixing being removed obtained in step (1), 60-65 DEG C is heated under stirring, instead
After answering 3-4 hours, filtering or centrifugation recycling catalyst, remaining reaction solution is after being evaporated off methanol, stratification, on
Layer liquid is biodiesel, and lower layer is glycerol.
The preferred soybean oil of grease, palm oil, peanut oil, rapeseed oil or gutter oil described in step (1);Sodium hydroxide is water-soluble
The concentration of liquid is 0.2-0.3mol/L, and the volume ratio of grease and sodium hydrate aqueous solution is 4:1;The preferred grease body of hexamethylene volume
Long-pending 1/3-1/4;
Catalyst described in step (2) is selected from the carbon material supported alkali of the above-mentioned polyaniline-coated biology of the present invention, and dosage is
The 0.5-0.8% of deacidification oil quality, except the mass ratio of acid lipid and methanol is 1:8-10.
Another embodiment of the present invention provides the carbon material supported alkali of above-mentioned polyaniline-coated biology and is preparing fatty acid methyl
Application in ester.
Another embodiment of the present invention provides a kind of preparation method of fatty acid methyl ester, it is characterised in that including walking as follows
It is rapid:
After fatty acid glycerine fat, methanol, catalyst are mixed, after 60-65 DEG C, reaction 3-4 hours is heated under stirring, mistake
Filter or centrifugation recycling catalyst, remaining reaction solution is after being evaporated off methanol, stratification, and supernatant liquid is fat
Sour methyl esters, lower layer are glycerol.
The catalyst is selected from the carbon material supported alkali of the above-mentioned polyaniline-coated biology of the present invention, and dosage is fatty acid glycerine
The mass ratio of the 0.5-0.8% of lipid amount, fatty acid glycerine fat and methanol is 1:8-10.
The preferred C16-C20 of the carbon chain lengths of fatty acid, fatty acid glycerine fat are further preferred in the fatty acid glycerine fat
Olein, tripalmitin;The olein is glyceryl monooleate, double oleins or three oleics
The mixing of one or more of ester;The tripalmitin is monopalmitin, double tripalmitins or three palms
The mixing of one or more of acid glyceride.
Compared with the prior art, the advantages of the present invention are as follows: (1) present invention by the method for ball milling keep polyaniline-coated raw
Object carbon material supported KF, K2CO3, a kind of novel solid body base is obtained, the solid base energy efficient catalytic grease (including fatty acid glycerine
Ester) and methanol between occur ester exchange reaction, prepare biodiesel;(2) polyaniline-coated biology of the present invention is carbon material supported
Base catalysis is high-efficient, easily separated, and can be recycled, and using 6 times, catalytic activity is basically unchanged.
Detailed description of the invention
Fig. 1 is nitrogen adsorption-desorption isotherm figure of product a;
Fig. 2 is the SEM figure of product A;
Fig. 3 is the SEM figure of product G.
Specific embodiment
For the ease of a further understanding of the present invention, examples provided below has done more detailed description to it.But
It is that these embodiments are only not supposed to be a limitation to the present invention or implementation principle for better understanding invention, reality of the invention
The mode of applying is not limited to the following contents.
Embodiment 1
(1) dry sweet potato leaves (400g) is taken, under nitrogen protection, after being warming up to 600 degree, carbonization 6 hours, natural cooling
To room temperature, biological carbon material is obtained;
(2) the biological carbon material (10g) for taking step (1) to obtain hydrochloric acid solution (1.0mol/L, 150mL) ultrasound
It after (30kHz) impregnates 5 hours, is added aniline (5mL), under ice bath, is added ammonium persulfate solution (0.5mol/L, 100mL), continues
10h is reacted under ice bath, filtering, washing of precipitate are drying to obtain polyaniline-coated biology carbon material (hereinafter referred to as product a).
Embodiment 2
(1) dry sweet potato leaves (400g) is taken, under nitrogen protection, after being warming up to 700 degree, carbonization 5 hours, natural cooling
To room temperature, biological carbon material is obtained;
(2) the biological carbon material (10g) for taking step (1) to obtain hydrochloric acid solution (2.0mol/L, 100mL) ultrasound
It after (40kHz) impregnates 4 hours, is added aniline (5mL), under ice bath, is added ammonium persulfate solution (1.0mol/L, 75mL), continues
6h is reacted under ice bath, filtering, washing of precipitate are drying to obtain polyaniline-coated biology carbon material (hereinafter referred to as product b).
Embodiment 3
Take product a (4g) and KF (4g), K2CO3(12g) mixing and ball milling is successively washed with water, dehydrated alcohol after 6 hours, in
It is dried in vacuo and is dried in vacuo for 24 hours up to the carbon material supported alkali (hereinafter referred to as product A) of polyaniline-coated biology under the conditions of 90 DEG C.
Embodiment 4
Take product b (3g) and KF (3g), K2CO3(9g) mixing and ball milling is successively washed with water, dehydrated alcohol after 6 hours, in
It is dried in vacuo and is dried in vacuo for 24 hours up to the carbon material supported alkali (hereinafter referred to as product B) of polyaniline-coated biology under the conditions of 90 DEG C.
Embodiment 5
It takes product a (4g) and KF (4g) after mixing and ball milling 6 hours, is successively washed with water, dehydrated alcohol, under the conditions of 90 DEG C
Vacuum drying is dried in vacuo to obtain the carbon material supported alkali (hereinafter referred to as products C) of polyaniline-coated biology for 24 hours.
Embodiment 6
Take product a (4g) and K2CO3(12g) mixing and ball milling is successively washed with water, dehydrated alcohol after 6 hours, in 90 DEG C of items
It is dried in vacuo under part and is dried in vacuo to obtain the carbon material supported alkali (hereinafter referred to as product D) of polyaniline-coated biology for 24 hours.
Embodiment 7
Take product a (4g) and KF (4g), K2CO3(4g) mixing and ball milling is successively washed with water, dehydrated alcohol after 6 hours, in
It is dried in vacuo under the conditions of 90 DEG C and is dried in vacuo to obtain the carbon material supported alkali (hereinafter referred to as product E) of polyaniline-coated biology for 24 hours.
Embodiment 8
The biological carbon material (4g) and KF (4g), K of 1 step of Example (1) preparation2CO3(12g) mixing and ball milling 6 hours
Afterwards, successively washed with water, dehydrated alcohol, be dried in vacuo under the conditions of 90 DEG C be dried in vacuo for 24 hours biological carbon material supported alkali (with
Lower abbreviation product F).
Embodiment 9
Product a (4g) is taken to be added containing KF (4g), K2CO3In the aqueous solution (200mL) of (12g), after stirring 24 hours, filtering,
Precipitating is successively washed with water, dehydrated alcohol, is dried in vacuo under the conditions of 90 DEG C and is dried in vacuo to obtain polyaniline-coated biology carbon materials for 24 hours
Material load alkali (hereinafter referred to as product G).
Embodiment 10
(1) it the deacidification processing of grease: takes soybean oil (60mL) that sodium hydrate aqueous solution (0.2mol/L, 15mL) is added, stirs
It after mixing 1.0h, is transferred in separatory funnel, stratification, collects supernatant liquid, after 50-55 DEG C of water washing to neutrality, be added
Hexamethylene (20mL), extra moisture is removed with water segregator, and finally vacuum distillation removes hexamethylene to get deacidification soybean oil;
(2) it after taking deacidification soybean oil (20g), methanol (160g) obtained in step (1), product A (160mg) to mix, stirs
It mixes down after being heated to 65 DEG C, reaction 3 hours, centrifugation recycling product A, remaining reaction solution is quiet after methanol is evaporated off
Layering is set, supernatant liquid is biodiesel (faint yellow), and lower layer is glycerol;Pass through gas Chromatographic Determination, the production of biodiesel
Rate is 96.3%.
According to the method for step (2), the product A of 5 recycling is recycled, catalytic activity is basically unchanged, the 6th secondary pollutant
The yield of diesel oil remains to reach 91.0%.
Embodiment 11
(1) it the deacidification processing of grease: takes gutter oil (100mL) that sodium hydrate aqueous solution (0.3mol/L, 25mL) is added, stirs
It after mixing 0.5h, is transferred in separatory funnel, stratification, collects supernatant liquid, after 55-60 DEG C of water washing to neutrality, be added
Hexamethylene (25mL), extra moisture is removed with water segregator, and finally vacuum distillation removes hexamethylene to get deacidification gutter oil;
(2) it after taking deacidification gutter oil (20g), methanol (200g) obtained in step (1), product B (100mg) to mix, stirs
It mixes down after being heated to 60 DEG C, reaction 4 hours, centrifugation recycling product B, remaining reaction solution is quiet after methanol is evaporated off
Layering is set, supernatant liquid is biodiesel (faint yellow), and lower layer is glycerol;Pass through gas Chromatographic Determination, the production of biodiesel
Rate is 94.3%;It is recycled the product B of recycling, the yield of the 6th secondary pollutant diesel oil is up to 89.8%.
Embodiment 12
According to the operation in 10 step of embodiment (2), respectively with etc. quality product B-G substitute products A, biodiesel
Yield see the table below.
Catalyst | Biodiesel production rate |
Product B | 94.7% |
Products C | 12.5% |
Product D | 37.3% |
Product E | 63.1% |
Product F | 42.6% |
Product G | 47.2% |
Embodiment 13
After taking olein (10g), methanol (80g), product A (80mg) to mix, 65 DEG C are heated under stirring, reaction
After 3 hours, centrifugation recycling product A, remaining reaction solution is after being evaporated off methanol, stratification, and supernatant liquid is
Biodiesel (faint yellow), lower layer are glycerol;By gas Chromatographic Determination, the yield of biodiesel is 95.6%.
Embodiment 14
After taking tripalmitin (10g), methanol (100g), product A (50mg) to mix, 60 DEG C are heated under stirring,
After reaction 4 hours, centrifugation recycling product B, remaining reaction solution is after being evaporated off methanol, stratification, supernatant liquid
As biodiesel (faint yellow), lower layer are glycerol;By gas Chromatographic Determination, the yield of biodiesel is 92.2%.
Claims (7)
1. a kind of polyaniline-coated biology carbon material, it is characterised in that the preparation method packet of the polyaniline-coated biology carbon material
Include following steps:
(1) dry sweet potato leaves are taken, under nitrogen protection, 600-700 degree is warming up to and naturally cools to room after carbonization 5-6 hours
Temperature obtains biological carbon material;
(2) after the biological carbon material hydrochloric acid solution ultrasound obtained step (1) is impregnated 4-5 hour, addition aniline, under ice bath,
Ammonium persulfate solution is added, 6-10h is reacted in continuation under ice bath, and filtering, is drying to obtain polyaniline-coated biological carbon at washing of precipitate
Material.
2. polyaniline-coated biology carbon material described in claim 1, it is characterised in that the concentration of hydrochloric acid described in step (2) is excellent
Select 1.0-2.0mol/L, every gram of biological carbon materials'use 10-15mL hydrochloric acid solution, every gram of biological carbon materials'use aniline 0.5mL,
Every milliliter of aniline uses 10-15mmol ammonium persulfate.
3. the described in any item polyaniline-coated biology carbon materials of claim 1-2, it is characterised in that over cure described in step (2)
The preferred 0.5-1.0mol/L of the concentration of acid ammonium solution.
4. the described in any item polyaniline-coated biology carbon materials of claim 1-3, it is characterised in that supersonic frequency in step (2)
For 30-40kHz.
5. the preparation method of the described in any item polyaniline-coated biology carbon materials of claim 1-4.
6. application of the described in any item polyaniline-coated biology carbon materials of claim 1-4 in load alkali.
7. application as claimed in claim 6, it is characterised in that the described in any item polyaniline-coated biology carbon materials of claim 1-4
Material and KF, K2CO3It after mixing and ball milling 6 hours, is successively washed with water, dehydrated alcohol, vacuum for 24 hours is dried in vacuo under the conditions of 90 DEG C
It is drying to obtain the carbon material supported alkali of polyaniline-coated biology.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201810743453.1A CN108927218A (en) | 2018-07-06 | 2018-07-06 | A kind of polyaniline-coated biology carbon material and its preparing the application in solid base |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201810743453.1A CN108927218A (en) | 2018-07-06 | 2018-07-06 | A kind of polyaniline-coated biology carbon material and its preparing the application in solid base |
Publications (1)
Publication Number | Publication Date |
---|---|
CN108927218A true CN108927218A (en) | 2018-12-04 |
Family
ID=64447957
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201810743453.1A Pending CN108927218A (en) | 2018-07-06 | 2018-07-06 | A kind of polyaniline-coated biology carbon material and its preparing the application in solid base |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN108927218A (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN109999910A (en) * | 2019-05-21 | 2019-07-12 | 扬州工业职业技术学院 | A kind of carbon material supported sulfonated polyaniline of biology and its application as catalyst |
CN113385163A (en) * | 2021-06-16 | 2021-09-14 | 西南林业大学 | Foam carbon heterogeneous solid base catalyst for grease transesterification and preparation method thereof |
Citations (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN1962824A (en) * | 2006-12-01 | 2007-05-16 | 湘潭大学 | Process for preparing supported solid catalyst for use in production of bio-diesel oil |
CN102430427A (en) * | 2011-09-20 | 2012-05-02 | 聊城大学 | Catalyst for preparing bio-diesel, preparation method and application thereof |
CN105948045A (en) * | 2016-07-18 | 2016-09-21 | 湘潭大学 | Preparation method and application of nitrogen-doped starch-based activated carbon microsphere material |
CN106430186A (en) * | 2016-09-16 | 2017-02-22 | 大连理工大学 | Preparation method and application of sweet potato leaf based active carbon |
CN106784704A (en) * | 2016-12-27 | 2017-05-31 | 陕西科技大学 | A kind of preparation method of N doping charcoal carbon negative pole material |
CN107200627A (en) * | 2017-05-18 | 2017-09-26 | 林云 | A kind of charcoal fertilizer and preparation method thereof |
CN107488111A (en) * | 2017-08-31 | 2017-12-19 | 扬州工业职业技术学院 | A kind of method of solid acid catalysis synthesizing gallic acid propyl ester |
-
2018
- 2018-07-06 CN CN201810743453.1A patent/CN108927218A/en active Pending
Patent Citations (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN1962824A (en) * | 2006-12-01 | 2007-05-16 | 湘潭大学 | Process for preparing supported solid catalyst for use in production of bio-diesel oil |
CN102430427A (en) * | 2011-09-20 | 2012-05-02 | 聊城大学 | Catalyst for preparing bio-diesel, preparation method and application thereof |
CN105948045A (en) * | 2016-07-18 | 2016-09-21 | 湘潭大学 | Preparation method and application of nitrogen-doped starch-based activated carbon microsphere material |
CN106430186A (en) * | 2016-09-16 | 2017-02-22 | 大连理工大学 | Preparation method and application of sweet potato leaf based active carbon |
CN106784704A (en) * | 2016-12-27 | 2017-05-31 | 陕西科技大学 | A kind of preparation method of N doping charcoal carbon negative pole material |
CN107200627A (en) * | 2017-05-18 | 2017-09-26 | 林云 | A kind of charcoal fertilizer and preparation method thereof |
CN107488111A (en) * | 2017-08-31 | 2017-12-19 | 扬州工业职业技术学院 | A kind of method of solid acid catalysis synthesizing gallic acid propyl ester |
Non-Patent Citations (6)
Title |
---|
DRELINKIEWICZ A ET AL: "Transesterification of triacetin and castor oil with methanol catalyzed by supported polyaniline-sulfate. A role of polymer morphology", 《APPLIED CATALYSIS A-GENERAL》 * |
KARIM, MOHAMMAD REZAUL ET AL: "Synthesis and characterization of conducting polyaniline-activated carbon nanocomposites", 《JOURNAL OF APPLIED POLYMER SCIENCE》 * |
XU ZHIHUI ET AL: "Oxygen Reduction Performance of the Nitrogen-Doped Carbon Materials Pyrolyzed from Polyaniline/Carbon Nanocage Composites", 《ACTA CHIMICA SINICA》 * |
徐泽杨 等: "HSO3-PAHAC固体酸催化大豆油酯交换合成生物柴油", 《现代化工》 * |
徐泽杨: "氮掺杂活性炭固体酸的制备及其催化有机合成反应", 《中国优秀硕士学位论文全文数据库 工程科技Ⅰ辑》 * |
靳福全: "生物柴油催化剂-KF/Ca-Al固体碱的制备及表征", 《现代化工》 * |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN109999910A (en) * | 2019-05-21 | 2019-07-12 | 扬州工业职业技术学院 | A kind of carbon material supported sulfonated polyaniline of biology and its application as catalyst |
CN113385163A (en) * | 2021-06-16 | 2021-09-14 | 西南林业大学 | Foam carbon heterogeneous solid base catalyst for grease transesterification and preparation method thereof |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
Dai et al. | Study of the microwave lipid extraction from microalgae for biodiesel production | |
Mukhtar et al. | Current status and challenges in the heterogeneous catalysis for biodiesel production | |
Ambat et al. | Recent advancement in biodiesel production methodologies using various feedstock: A review | |
Avhad et al. | A review on recent advancement in catalytic materials for biodiesel production | |
Qu et al. | Microwave-assisted in-situ transesterification of Spirulina platensis to biodiesel using PEG/MgO/ZSM-5 magnetic catalyst | |
Vadery et al. | Room temperature production of jatropha biodiesel over coconut husk ash | |
KR101134294B1 (en) | Oil extraction and biodiesel production from microalgae | |
CN101249449A (en) | Novel solid body base catalyst and applications for biological diesel oil synthesizing | |
CN102744053B (en) | Composite solid base CaO-Al2O3 and method for preparing biodiesel oil by catalysis of waste vegetable oil with the same | |
Tang et al. | Highly active CaO for the transesterification to biodiesel production from rapeseed oil | |
CN1962824A (en) | Process for preparing supported solid catalyst for use in production of bio-diesel oil | |
CN103370405A (en) | Improved process for the preparation of fatty acid alkyl esters (biodiesel) from triglyceride oils using eco-friendly solid base catalysts | |
CN101249431A (en) | Novel solid body base catalyst and applications thereof in biological diesel oil synthesizing | |
CN108927218A (en) | A kind of polyaniline-coated biology carbon material and its preparing the application in solid base | |
Asri et al. | Utilization of eggshell waste as low-cost solid base catalyst for biodiesel production from used cooking oil | |
CN108927217A (en) | A kind of solid base catalyst based on polyaniline-coated carbon material and its application in preparation biodiesel | |
CN102172521B (en) | Solid basic catalyst and preparation method and application thereof | |
CN1916115A (en) | Method for producing biological diesel oil through ester interchange accelerated by microwave | |
KR102499622B1 (en) | Solid acid catalyst for biodiesel production, solid base catalyst for biodiesel production, methods for preparing the same, and methods for producing biodiesel using the same | |
CN108795578A (en) | A method of utilizing catalyzed by solid base preparing biodiesel by ester exchange | |
KR101411952B1 (en) | Solid acid catalyst and method for preparing biodiesel using the catalyst | |
CN106000436A (en) | Preparation method of heterogeneous catalyst with camphor tree ash as carrier and application thereof | |
Lukić et al. | Adsorptive pretreatment of waste cooking oil using quicklime for fatty acid methyl esters synthesis | |
Islam et al. | Advanced technologies in biodiesel: New advances in designed and optimized catalysts | |
CN101249454A (en) | Solid base catalyst and applications for preparing biological diesel oil |
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 |