CN105692618A - Production method of biomass-powder activated carbon - Google Patents
Production method of biomass-powder activated carbon Download PDFInfo
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- CN105692618A CN105692618A CN201610090543.6A CN201610090543A CN105692618A CN 105692618 A CN105692618 A CN 105692618A CN 201610090543 A CN201610090543 A CN 201610090543A CN 105692618 A CN105692618 A CN 105692618A
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- Prior art keywords
- activated carbon
- drying
- seconds
- neutral
- production method
- 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.)
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- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 title claims abstract description 46
- 238000004519 manufacturing process Methods 0.000 title claims abstract description 14
- 239000000843 powder Substances 0.000 title abstract 3
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 26
- 238000010438 heat treatment Methods 0.000 claims abstract description 24
- 238000001035 drying Methods 0.000 claims abstract description 21
- 238000000034 method Methods 0.000 claims abstract description 21
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 claims abstract description 20
- KWYUFKZDYYNOTN-UHFFFAOYSA-M Potassium hydroxide Chemical compound [OH-].[K+] KWYUFKZDYYNOTN-UHFFFAOYSA-M 0.000 claims abstract description 18
- 235000009496 Juglans regia Nutrition 0.000 claims abstract description 16
- 235000020234 walnut Nutrition 0.000 claims abstract description 16
- SQGYOTSLMSWVJD-UHFFFAOYSA-N silver(1+) nitrate Chemical compound [Ag+].[O-]N(=O)=O SQGYOTSLMSWVJD-UHFFFAOYSA-N 0.000 claims abstract description 15
- 239000012153 distilled water Substances 0.000 claims abstract description 10
- 230000007935 neutral effect Effects 0.000 claims abstract description 10
- 238000002156 mixing Methods 0.000 claims abstract description 8
- 239000002245 particle Substances 0.000 claims abstract description 7
- AXCZMVOFGPJBDE-UHFFFAOYSA-L calcium dihydroxide Chemical compound [OH-].[OH-].[Ca+2] AXCZMVOFGPJBDE-UHFFFAOYSA-L 0.000 claims abstract description 6
- 239000000920 calcium hydroxide Substances 0.000 claims abstract description 6
- 229910001861 calcium hydroxide Inorganic materials 0.000 claims abstract description 6
- 230000005855 radiation Effects 0.000 claims abstract description 6
- 239000011363 dried mixture Substances 0.000 claims abstract description 3
- 240000007049 Juglans regia Species 0.000 claims abstract 2
- 239000002028 Biomass Substances 0.000 claims description 11
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 claims description 10
- 238000003763 carbonization Methods 0.000 claims description 10
- 239000008187 granular material Substances 0.000 claims description 9
- 239000007788 liquid Substances 0.000 claims description 6
- 229910052757 nitrogen Inorganic materials 0.000 claims description 5
- 238000011010 flushing procedure Methods 0.000 claims description 3
- 238000007654 immersion Methods 0.000 claims description 2
- 238000003756 stirring Methods 0.000 claims description 2
- 239000000203 mixture Substances 0.000 abstract description 7
- 239000000126 substance Substances 0.000 abstract description 7
- 238000002791 soaking Methods 0.000 abstract description 6
- 238000001816 cooling Methods 0.000 abstract description 4
- 238000005342 ion exchange Methods 0.000 abstract description 4
- 239000011148 porous material Substances 0.000 abstract description 4
- 239000003054 catalyst Substances 0.000 abstract description 3
- 238000010521 absorption reaction Methods 0.000 abstract 1
- 238000001914 filtration Methods 0.000 abstract 1
- 230000001007 puffing effect Effects 0.000 abstract 1
- 238000005406 washing Methods 0.000 abstract 1
- 241000758789 Juglans Species 0.000 description 14
- 239000002131 composite material Substances 0.000 description 3
- 230000007613 environmental effect Effects 0.000 description 3
- 239000002994 raw material Substances 0.000 description 3
- 239000003507 refrigerant Substances 0.000 description 3
- 239000010420 shell particle Substances 0.000 description 3
- 239000006227 byproduct Substances 0.000 description 2
- 235000013399 edible fruits Nutrition 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 235000013372 meat Nutrition 0.000 description 2
- 210000000582 semen Anatomy 0.000 description 2
- RBTBFTRPCNLSDE-UHFFFAOYSA-N 3,7-bis(dimethylamino)phenothiazin-5-ium Chemical compound C1=CC(N(C)C)=CC2=[S+]C3=CC(N(C)C)=CC=C3N=C21 RBTBFTRPCNLSDE-UHFFFAOYSA-N 0.000 description 1
- ZCYVEMRRCGMTRW-UHFFFAOYSA-N 7553-56-2 Chemical compound [I] ZCYVEMRRCGMTRW-UHFFFAOYSA-N 0.000 description 1
- 101710134784 Agnoprotein Proteins 0.000 description 1
- 244000144725 Amygdalus communis Species 0.000 description 1
- 235000011437 Amygdalus communis Nutrition 0.000 description 1
- 241000758791 Juglandaceae Species 0.000 description 1
- 239000012190 activator Substances 0.000 description 1
- 239000003463 adsorbent Substances 0.000 description 1
- 235000020224 almond Nutrition 0.000 description 1
- 230000000844 anti-bacterial effect Effects 0.000 description 1
- 239000003575 carbonaceous material Substances 0.000 description 1
- 239000003610 charcoal Substances 0.000 description 1
- 230000001186 cumulative effect Effects 0.000 description 1
- 230000018109 developmental process Effects 0.000 description 1
- 239000003814 drug Substances 0.000 description 1
- 238000003912 environmental pollution Methods 0.000 description 1
- 235000013305 food Nutrition 0.000 description 1
- 229910052740 iodine Inorganic materials 0.000 description 1
- 239000011630 iodine Substances 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 238000005272 metallurgy Methods 0.000 description 1
- 229960000907 methylthioninium chloride Drugs 0.000 description 1
- 235000015097 nutrients Nutrition 0.000 description 1
- 239000003960 organic solvent Substances 0.000 description 1
- 230000008929 regeneration Effects 0.000 description 1
- 238000011069 regeneration method Methods 0.000 description 1
- 238000001179 sorption measurement Methods 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
- 239000003799 water insoluble solvent Substances 0.000 description 1
Classifications
-
- A—HUMAN NECESSITIES
- A01—AGRICULTURE; FORESTRY; ANIMAL HUSBANDRY; HUNTING; TRAPPING; FISHING
- A01N—PRESERVATION OF BODIES OF HUMANS OR ANIMALS OR PLANTS OR PARTS THEREOF; BIOCIDES, e.g. AS DISINFECTANTS, AS PESTICIDES OR AS HERBICIDES; PEST REPELLANTS OR ATTRACTANTS; PLANT GROWTH REGULATORS
- A01N59/00—Biocides, pest repellants or attractants, or plant growth regulators containing elements or inorganic compounds
- A01N59/16—Heavy metals; Compounds thereof
-
- B01J35/618—
-
- B01J35/635—
-
- B01J35/638—
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01P—INDEXING SCHEME RELATING TO STRUCTURAL AND PHYSICAL ASPECTS OF SOLID INORGANIC COMPOUNDS
- C01P2006/00—Physical properties of inorganic compounds
- C01P2006/12—Surface area
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01P—INDEXING SCHEME RELATING TO STRUCTURAL AND PHYSICAL ASPECTS OF SOLID INORGANIC COMPOUNDS
- C01P2006/00—Physical properties of inorganic compounds
- C01P2006/14—Pore volume
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01P—INDEXING SCHEME RELATING TO STRUCTURAL AND PHYSICAL ASPECTS OF SOLID INORGANIC COMPOUNDS
- C01P2006/00—Physical properties of inorganic compounds
- C01P2006/40—Electric properties
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01P—INDEXING SCHEME RELATING TO STRUCTURAL AND PHYSICAL ASPECTS OF SOLID INORGANIC COMPOUNDS
- C01P2006/00—Physical properties of inorganic compounds
- C01P2006/90—Other properties not specified above
Abstract
The invention discloses a production method of biomass-powder activated carbon and relates to the technical field of activated carbon. The production method includes: drying walnut shells, crushing into particles, mixing the particles with calcium hydroxide and potassium hydroxide according to the mass ratio of 1:1-5:0.05-0.20, soaking with water, puffing, drying, heating the dried mixture with a microwave radiation method, cooling, soaking with hydrochloric acid, rinsing the soaked mixture with distilled water until the same is neutral, and drying; mixing the dried substances with AgNO3 solution for soaking, filtering, washing with distilled water until the soaked substances is neutral, processing with steam water, and drying. The production method has the advantages that the biomass-powder activated carbon produced by the method has continuous cavity ducts, even pore diameters and extremely large specific surface area, the cavities and ducts account for 50% of the total size of the activated carbon, so that the activated carbon has strong ion exchanging ability and absorption ability; the activated carbon has large ion exchanging capacity and is loaded with catalyst Ag and capable of absorbing harmful substances and moisture in air.
Description
Technical field
The present invention relates to activated carbon manufacture technology field, the manufacture method of especially a kind of powdered biomass activated carbon。
Background technology
Activated carbon is a kind of porous carbonaceous material with flourishing pore structure and bigger serface, its physical and chemical performance is stable, mechanical strength is high, water insoluble and organic solvent, there is advantages such as being easy to regeneration, it is adsorbent and the catalyst carrier of a kind of function admirable, thus being widely used in the fields such as food processing, metallurgy, medicine, chemical industry, military affairs, environmental protection and the energy。The pore structure of activated carbon determines its physical and chemical performance, and owing to agricultural by-products amount charcoal processing rate big, inexpensive is high, and utilization economizes on resources and environmental protection, and therefore, many agricultural by-products may often be such that the primary raw material for preparing activated carbon。Walnut shell, also known as Semen Juglandis, Qiang's Fructus Persicae, for juglandaceae plant。With almond, Fructus anacardii, Semen coryli heterophyllae be called world-renowned " four big dry fruits "。Walnut shell and meat contains abundant nutrient, is the dry fruits liked of people, and after walnut shell takes off walnut shell and meat, remaining walnut shell, people, often when it is arbitrarily abandoned by rubbish, not only waste resource, also result in sanitary fill。At present, not yet find to utilize walnut shell as primary raw material and corresponding activator to prepare the report of powdered biological activated carbon。
Summary of the invention
Problem to be solved by this invention be to provide a kind of can the manufacture method of powdered biomass activated carbon of resource reutilization。
In order to solve the problems referred to above, the technical solution used in the present invention is:
Its method is for being ground into granule after being dried by walnut shell, this granule is mixed with the ratio that calcium hydroxide and potassium hydroxide are 1:1-5:0.05-0.20 in mass ratio, add water immersion, dry after expanded, dried mixture microwave irradiation is heated, then cools down, then soak with hydrochloric acid stirring, then with distilled water rinsing to neutral, dry;By drying object and AgNO3Solution mixing is soaked, and filters, then with distilled water flushing to neutral, then processes by steam water, final drying。
In technique scheme, scheme is it may also is that described drying is the heating, drying through 70 ° of C-100 ° of C more specifically;The particle diameter of described granule is 900-1200 order;The described time soaked is 3-5 hour;The concentration of described hydrochloric acid is 1.5mol/L, and the time adding soak with hydrochloric acid is 12 hours;Described AgNO3The concentration of solution is 0.05mol/L, described drying object and AgNO3Solution presses solid-to-liquid ratio 1:5;The temperature of described steam water is 180-200 DEG C, and the time that steam water processes is 2 hours。
Further: described microwave radiation heating process adopts nitrogen protection, first with heating rate for 10 ° of C/ seconds, heat to 230 ° of C-300 ° of C; rotate carbonization 30 seconds-50 seconds; then again with heating rate for 5 ° of C/ seconds, heat to 600 ° of C-800 ° of C, rotate carbonization 60 seconds-90 seconds。
Owing to have employed technique scheme, the present invention compared with prior art has the advantages that
1, the powdered biomass activated carbon that the present invention makes is adopted to have continuous print cavity passage, having the more uniform aperture of ratio, have great specific surface area, hole and duct account for the 50% of cumulative volume, make it have stronger ion-exchange capacity and absorbability, be good adsorbing material and antibacterial;There is relatively larger ion exchange capacity, and be loaded with catalyst Ag, it is possible to harmful substance in absorbed air and moisture。
2, using discarded walnut shell as raw material, it is to avoid the wasting of resources and decrease environmental pollution, there is environmental protection and promote the sound development of industry, and then widening plantation family and increase income channel。
Detailed description of the invention
Below in conjunction with specific embodiment, the invention will be further described:
Embodiment 1:
The manufacture method of the powdered biomass activated carbon of the present embodiment, comprises the steps:
A, first by walnut shell after the heating, drying of 70 ° of C, then be crushed to, with pulverizer, the granule that particle diameter is 900 orders;
B, by step A walnut shell particle and the calcium hydroxide prepared and potassium hydroxide, ratio for 1:1:0.20 is stirred mix in mass ratio, and adds that the water retting that can just be completely sunk in the water by mixture 3 hours is expanded rear to be dried;
C, the drying composite of step B gained is placed in classification tubular heater, adopt microwave irradiation heating, natural cooling subsequently;
D, the hydrochloric acid that step C prepares refrigerant 1.5mol/L are that 1:10 mixing is soaked by solid-to-liquid ratio, are stirred soaking, when being stirred continuously through the process of 12 hours, filter, then with distilled water rinsing to neutral, dry;AgNO by drying object Yu 0.05mol/L3Solution soaks by solid-to-liquid ratio 1:5 mixing, lower processed through 2 hours being stirred continuously, filters, then with distilled water flushing to neutral, shifts as in autoclave, through 180 DEG C of steam treatment 2 hours, takes out, dry;
Step C microwave radiation heating process adopts nitrogen protection, first with heating rate for 10 ° of C/ seconds, heats to 230 ° of C, rotate carbonization 50 seconds, then again with heating rate for 5 ° of C/ seconds, heat to 600 ° of C, rotate carbonization 90 seconds。
Embodiment 2:
The manufacture method of the powdered biomass activated carbon of the present embodiment, comprises the steps:
A, first by walnut shell after the heating, drying of 80 ° of C, then be crushed to, with pulverizer, the granule that particle diameter is 1000 orders;
B, by step A walnut shell particle and the calcium hydroxide prepared and potassium hydroxide, ratio for 1:3:0.05 is stirred mix in mass ratio, and adds that the water retting that can just be completely sunk in the water by mixture 4 hours is expanded rear to be dried;
C, the drying composite of step B gained is placed in classification tubular heater, adopt microwave irradiation heating, natural cooling subsequently;
D, by step C prepare refrigerant 1.5mol/L hydrochloric acid by solid-to-liquid ratio be 1:10 mixing soak, it is stirred soaking, when being stirred continuously through the process of 12 hours, filter, then with distilled water rinsing to neutral, dry, transfer is as in autoclave, through 200 DEG C of steam treatment 2 hours, take out, dry;
Step C microwave radiation heating process adopts nitrogen protection, first with heating rate for 10 ° of C/ seconds, heats to 230 ° of C, rotate carbonization 50 seconds, then again with heating rate for 5 ° of C/ seconds, heat to 600 ° of C, rotate carbonization 90 seconds。
Embodiment 3:
The manufacture method of the powdered biomass activated carbon of the present embodiment, comprises the steps:
A, first by walnut shell after the heating, drying of 100 ° of C, then be crushed to, with pulverizer, the granule that particle diameter is 1200 orders;
B, by step A walnut shell particle and the calcium hydroxide prepared and potassium hydroxide, ratio for 1:5:0.15 is stirred mix in mass ratio, and adds that the water retting that can just be completely sunk in the water by mixture 5 hours is expanded rear to be dried;
C, the drying composite of step B gained is placed in classification tubular heater, adopt microwave irradiation heating, natural cooling subsequently;
D, by step C prepare refrigerant 1.5mol/L hydrochloric acid by solid-to-liquid ratio be 1:10 mixing soak, it is stirred soaking, when being stirred continuously through the process of 12 hours, filter, then with distilled water rinsing to neutral, dry, transfer is as in autoclave, through 200 DEG C of steam treatment 2 hours, take out, dry;
Step C microwave radiation heating process adopts nitrogen protection, first with heating rate for 10 ° of C/ seconds, heats to 230 ° of C, rotate carbonization 50 seconds, then again with heating rate for 5 ° of C/ seconds, heat to 600 ° of C, rotate carbonization 90 seconds。
The specific surface area of the powdered biomass activated carbon that the employing present invention prepares is: 1530-2450m2/ g, micropore specific area accounts for more than 99%, and pore volume is: 0.62-1.16cm3/ g, iodine number is 845-1545mg/g, and methylene blue adsorption value is: 10-21ml/0.1g, ash≤0.15%, and resistance value is 0.3-0.6 Ω。
Claims (3)
1. the manufacture method of a powdered biomass activated carbon, it is characterised in that:
It is ground into granule after being dried by walnut shell, this granule is mixed with the ratio that calcium hydroxide and potassium hydroxide are 1:1-5:0.05-0.20 in mass ratio, add water immersion, dry after expanded, dried mixture microwave irradiation is heated, then cools down, then soak with hydrochloric acid stirring, then with distilled water rinsing to neutral, dry;By drying object and AgNO3Solution mixing is soaked, and filters, then with distilled water flushing to neutral, then processes by steam water, final drying。
2. the manufacture method of powdered biomass activated carbon according to claim 1, it is characterised in that:
Described drying is the heating, drying through 70 ° of C-100 ° of C;The particle diameter of described granule is 900-1200 order;The described time soaked is 3-5 hour;The concentration of described hydrochloric acid is 1.5mol/L, and the time adding soak with hydrochloric acid is 12 hours;Described AgNO3The concentration of solution is 0.05mol/L, described drying object and AgNO3Solution presses solid-to-liquid ratio 1:5;The temperature of described steam water is 180-200 DEG C, and the time that steam water processes is 2 hours。
3. the manufacture method of powdered biomass activated carbon according to claim 1 and 2; it is characterized in that: described microwave radiation heating process adopts nitrogen protection; first with heating rate for 10 ° of C/ seconds; heat to 230 ° of C-300 ° of C; rotate carbonization 30 seconds-50 seconds; then again with heating rate for 5 ° of C/ seconds, heat to 600 ° of C-800 ° of C, rotate carbonization 60 seconds-90 seconds。
Priority Applications (1)
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CN201610090543.6A CN105692618A (en) | 2016-02-18 | 2016-02-18 | Production method of biomass-powder activated carbon |
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CN201610090543.6A CN105692618A (en) | 2016-02-18 | 2016-02-18 | Production method of biomass-powder activated carbon |
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CN201610090543.6A Pending CN105692618A (en) | 2016-02-18 | 2016-02-18 | Production method of biomass-powder activated carbon |
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Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN106118199A (en) * | 2016-06-28 | 2016-11-16 | 陈建峰 | A kind of preparation method of coating dedicated biomass antistatic filler |
CN106609477A (en) * | 2016-11-14 | 2017-05-03 | 蚌埠市风驰滤清器有限公司 | An oil-proof filter paper for filters |
CN106744801A (en) * | 2016-12-26 | 2017-05-31 | 新昌县钧国生物技术有限公司 | Bud rate biomass carbon nursery material occurred frequently and preparation method and application |
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CN1309090A (en) * | 2000-02-14 | 2001-08-22 | 苏才元 | Nm-class material, process for preparing it from activated carbon and its use |
CN1876927A (en) * | 2006-06-28 | 2006-12-13 | 陆书明 | Silver-supported active carbon cloth and production method thereof |
CN103803548A (en) * | 2014-02-20 | 2014-05-21 | 江西师范大学 | Biomass powdered activated carbon prepared from lychee seeds and preparation method thereof |
CN104445195A (en) * | 2014-12-08 | 2015-03-25 | 柳州东侯生物能源科技有限公司 | Preparation method of powdered biomass activated carbon by using longan seeds |
-
2016
- 2016-02-18 CN CN201610090543.6A patent/CN105692618A/en active Pending
Patent Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
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CN1309090A (en) * | 2000-02-14 | 2001-08-22 | 苏才元 | Nm-class material, process for preparing it from activated carbon and its use |
CN1876927A (en) * | 2006-06-28 | 2006-12-13 | 陆书明 | Silver-supported active carbon cloth and production method thereof |
CN103803548A (en) * | 2014-02-20 | 2014-05-21 | 江西师范大学 | Biomass powdered activated carbon prepared from lychee seeds and preparation method thereof |
CN104445195A (en) * | 2014-12-08 | 2015-03-25 | 柳州东侯生物能源科技有限公司 | Preparation method of powdered biomass activated carbon by using longan seeds |
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刘玉荣: "《碳材料在超级电容器中的应用》", 31 January 2013, 国防工业出版社 * |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN106118199A (en) * | 2016-06-28 | 2016-11-16 | 陈建峰 | A kind of preparation method of coating dedicated biomass antistatic filler |
CN106609477A (en) * | 2016-11-14 | 2017-05-03 | 蚌埠市风驰滤清器有限公司 | An oil-proof filter paper for filters |
CN106744801A (en) * | 2016-12-26 | 2017-05-31 | 新昌县钧国生物技术有限公司 | Bud rate biomass carbon nursery material occurred frequently and preparation method and application |
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Application publication date: 20160622 |