CN108455598A - A kind of method that antibiotic bacterium dregs prepare the high performance active carbon rich in micropore - Google Patents
A kind of method that antibiotic bacterium dregs prepare the high performance active carbon rich in micropore Download PDFInfo
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- CN108455598A CN108455598A CN201810140010.3A CN201810140010A CN108455598A CN 108455598 A CN108455598 A CN 108455598A CN 201810140010 A CN201810140010 A CN 201810140010A CN 108455598 A CN108455598 A CN 108455598A
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- micropore
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Abstract
The present invention provides a kind of method that antibiotic bacterium dregs prepare the high performance active carbon rich in micropore, belongs to antibiotic bacterium dregs resource technology field.This method is first by the antibiotic bacterium dregs of pending moisture content 70% 90%, and after adding alkali to adjust pH, stirring stands filtering;Then by the solid matter being obtained by filtration by be dried in vacuo dry, and it is levigate be 0.1 2mm sizes particle;Finally, the dry powder after will be levigate is heated to 400 550 DEG C with 10 20 DEG C/min heating rates in tube furnace, in CO2It is pyrolyzed 3 6h in atmosphere, obtains the activated carbon rich in micropore.This method is simple and practicable, can be efficiently used to antibiotic bacterium dregs, and activated carbon obtained is rich in micropore, there is great utility value.
Description
Technical field
The present invention relates to antibiotic bacterium dregs resource technology field, particularly relate to a kind of antibiotic bacterium dregs and prepare be rich in micropore
High performance active carbon method.
Background technology
China is maximum antibiotic primary producing country and exported country in the world, domestic product antibiotic yield 12 in 2013
Ten thousand tons, 30,000 tons of middle outlet accounts for the 70% of world market.The large-scale production of antibiotic also produces a large amount of antibiosis simultaneously
Plain bacteria residue.Because they contain, there are many noxious materials (such as antibiotic residues, heavy metal and Metabolic Intermediate), are arranged within 2002
Enter《Forbid the types of drugs catalogue used in feed and animal drinking water》, it is put within 2008《National Hazard waste name
Record》.Many researchs find that the antibiotic residue being exposed in natural environment can lead to the generation of antibiotic resistant bacteria.It defends in the world
Raw tissue (WHO) reports that antibiotic resistant bacteria has occurred and propagated in human and animal.Fresh antibiotic bacteria residue property is not
Stabilization, easily corruption simultaneously distribute stench, and finally threaten human health.Therefore, how antibiotic bacterium dregs safely and effectively to be handled
As the previous urgent problem of mesh.
The existing frequently-used bacteria residue treatment technology of pharmacy corporation is security landfill and burning, and security landfill is to put hazardous waste
A kind of disposal options in the soil are set or stored, the purpose is to bury or change the characteristic of hazardous waste, are suitable for disposition not
The hazardous waste of useful constituent or energy can be recycled.Since antibiotic bacterium dregs moisture content is high, security landfill is directly carried out, is deposited
The problems such as taking up a large area, cost of disposal is high and percolate, and it can result in waste of resources.Burning be it is a kind of most thoroughly, answer
With widest processing disposal technology, harmful components can be used with pyrolytic by most of pharmaceutical factory.But due to bacteria residue
Middle N element content is high, is several times to more than ten times of coal, unavoidably will produce a large amount of NOx, deal with improperly and easily cause environment
Problem.It is low additionally, due to its moisture content height, calorific value so that processing cost reaches 2000 yuan/t or so, seriously constrains pharmacy enterprise
The sound development of industry.Therefore, how economically and safely to handle and recycling antibiotic bacterium dregs are that pharmacy corporation is urgently to be resolved hurrily at present
Major issue.
Contain more rich organic matter in antibiotic bacterium dregs, such as crude fat, crude protein, carbohydrate, by pyrolytic technique,
Under conditions of anaerobic or anoxic, the larger molecular organics in bacteria residue can be made to be cracked into flammable micro-molecular gas (H2、CH4And CO
Deng), the methanol of liquid, acetone, acetic acid, acetaldehyde, tar, solvent naphtha and fixed carbon (coke, carbon black) etc., above-mentioned product can return
It receives and utilizes.Therefore, bacteria residue pyrolysis, which prepares activated carbon, has very big potentiality.
Application No. is 201310051119.7 patents to carry out activation system using ionic liquid and metal to antibiotic bacterium dregs
Standby activated carbon.Application No. is 201110388856.7 patents to prepare activated carbon using penicillin or terramycin, can be to bacteria residue
Carry out recycling treatment.But experiment finds that there are a large amount of protein in bacteria residue, the part is easy to cave in pyrolytic process
Deformation is unfavorable for the formation of micropore so that pore structure reduction.Bacteria residue is etched using containing aqueous slkali, removes part
After protein component, the high performance active carbon rich in micropore can be generated by carrying out activation.
Invention content
The technical problem to be solved in the present invention is to provide a kind of antibiotic bacterium dregs to prepare the high performance active carbon rich in micropore
Method.
It is as follows that the method comprising the steps of:
(1) by the antibiotic bacterium dregs that pending moisture content is 70%-90%, add lye to adjust pH to 8.0-10.0, stir
0.5-2h is mixed, is filtered after standing 6-10h;
(2) solid matter being obtained by filtration in step (1) is dried under the conditions of 30-70 DEG C by being dried in vacuo, is obtained
Bacteria residue dry powder;
(3) the levigate particle for 0.1-2mm of bacteria residue dry powder after drying step (2);
(4) bacteria residue dry powder particle of the step (3) after levigate is heated to 10-20 DEG C/min heating rates in tube furnace
400-550 DEG C, in CO2It is pyrolyzed 3-6h in atmosphere, obtains the activated carbon rich in micropore.
Wherein, the antibiotic bacterium dregs in step (1) are ospeneff, gentamicin, one kind in streptomysin bacteria residue or several
Kind.
Lye in step (1) is one or both of sodium hydroxide, potassium hydroxide.
Alternatively, the lye in step (1) is Ca (OH)2The mixed liquor prepared with one or both of NaCl or KCl,
Middle Ca (OH)2Molar ratio with NaCl or KCl is 0.5-0.6:1.
Above two concentration of lye is with OH-Densimeter is 0.2-2mol/L.
The above-mentioned technical proposal of the present invention has the beneficial effect that:
This method is simple and practicable, can be efficiently used to antibiotic bacterium dregs, and activated carbon obtained is rich in micropore, has
Great utility value.
Description of the drawings
Fig. 1 is that the antibiotic bacterium dregs of the present invention prepare the method and process flow chart of the high performance active carbon rich in micropore.
Specific implementation mode
To keep the technical problem to be solved in the present invention, technical solution and advantage clearer, below in conjunction with attached drawing and tool
Body embodiment is described in detail.
The present invention provides a kind of method that antibiotic bacterium dregs prepare the high performance active carbon rich in micropore.
As shown in Figure 1, this method the specific steps are:
(1) by the antibiotic bacterium dregs that pending moisture content is 70%-90%, add lye to adjust pH to 8.0-10.0, stir
0.5-2h is mixed, is filtered after standing 6-10h;
(2) solid matter being obtained by filtration in step (1) is dried under the conditions of 30-70 DEG C by being dried in vacuo, is obtained
Bacteria residue dry powder;
(3) the levigate particle for 0.1-2mm of bacteria residue dry powder after drying step (2);
(4) bacteria residue dry powder particle of the step (3) after levigate is heated to 10-20 DEG C/min heating rates in tube furnace
400-550 DEG C, in CO2It is pyrolyzed 3-6h in atmosphere, obtains the activated carbon rich in micropore.
It is explained with reference to specific embodiment.
Embodiment 1
Sodium hydroxide (NaOH) solution tune of concentration 0.2mol/L is added in the penicillin mushroom dregs of certain pharmaceutical factory's moisture content 78%
Section stirs 0.5h to pH value 8, is filtered after standing 10h.The solid being obtained by filtration is passed through into vacuum drying, mill under the conditions of 30 DEG C
Thin is the particle of 0.1mm sizes, dry powder is heated to 550 DEG C with 20 DEG C/min heating rates in tube furnace, in CO2In atmosphere
It is pyrolyzed 3h, it is 537m to obtain specific surface area2The activated carbon of/g, yield 29.2%.
Embodiment 2
The streptomysin bacteria residue of certain pharmaceutical factory's moisture content 70%, potassium hydroxide (KOH) solution that concentration 2mol/L is added are adjusted
To pH value 10, mechanical agitation 2h is filtered after standing 6h.The solid being obtained by filtration is dried under the conditions of 30 DEG C by being dried in vacuo
Dry, dry powder is heated to 550 DEG C, in CO by the levigate particle for 0.1mm sizes with 10 DEG C/min heating rates in tube furnace2
6h is pyrolyzed in atmosphere, it is 792m to obtain specific surface area2The activated carbon of/g, yield 27.5%.
Embodiment 3
The Ca (OH) of concentration 2mol/L is added in the gentamicin bacteria residue of certain pharmaceutical factory's moisture content 81%2With the mixing of NaCl
Liquid, mixing ratio 0.5:1, it is adjusted to pH value 10, stirs 0.5h, is filtered after standing 6h.By the solid being obtained by filtration in 70 DEG C of items
It is dried under part by being dried in vacuo, the levigate particle for 2mm sizes, dry powder is added with 20 DEG C/min heating rates in tube furnace
Heat is to 400 DEG C, in CO26h is pyrolyzed in atmosphere, it is 890m to obtain specific surface area2The activated carbon of/g, yield 24.9%.
Embodiment 4
The Ca (OH) of concentration 0.2mol/L is added in the ospeneff bacteria residue of certain pharmaceutical factory's moisture content 90%2With mixing for NaCl
Close liquid, mixing ratio 0.6:1, it is adjusted to pH value 8, mechanical agitation 0.5h is filtered after standing 6h.By the solid being obtained by filtration 70
It is dried under the conditions of DEG C by being dried in vacuo, the levigate particle for 2mm sizes, by dry powder with 10 DEG C/min heating rates in tube furnace
In be heated to 550 DEG C, in CO22h is pyrolyzed in atmosphere, it is 605m to obtain specific surface area2The activated carbon of/g, yield 26.6%.
The above is the preferred embodiment of the present invention, it is noted that for those skilled in the art
For, without departing from the principles of the present invention, several improvements and modifications can also be made, these improvements and modifications
It should be regarded as protection scope of the present invention.
Claims (5)
1. a kind of method that antibiotic bacterium dregs prepare the high performance active carbon rich in micropore, it is characterised in that:Including steps are as follows:
(1) by the antibiotic bacterium dregs that pending moisture content is 70%-90%, lye is added to adjust pH to 8.0-10.0, stirring
0.5-2h is filtered after standing 6-10h;
(2) solid matter being obtained by filtration in step (1) is dried under the conditions of 30-70 DEG C by being dried in vacuo, obtains bacteria residue
Dry powder;
(3) the levigate particle for 0.1-2mm of bacteria residue dry powder after drying step (2);
(4) bacteria residue dry powder particle of the step (3) after levigate is heated to 400- with 10-20 DEG C/min heating rates in tube furnace
550 DEG C, in CO2It is pyrolyzed 3-6h in atmosphere, obtains the activated carbon rich in micropore.
2. the method that antibiotic bacterium dregs according to claim 1 prepare the high performance active carbon rich in micropore, feature exist
In:Antibiotic bacterium dregs in the step (1) are one or more of ospeneff, gentamicin, streptomysin bacteria residue.
3. the method that antibiotic bacterium dregs according to claim 1 prepare the high performance active carbon rich in micropore, feature exist
In:Lye in the step (1) is one or both of sodium hydroxide, potassium hydroxide.
4. the method that antibiotic bacterium dregs according to claim 1 prepare the high performance active carbon rich in micropore, feature exist
In:Lye in the step (1) is Ca (OH)2The mixed liquor prepared with one or both of NaCl or KCl, wherein Ca
(OH)2Molar ratio with NaCl or KCl is 0.5-0.6:1.
5. the method that antibiotic bacterium dregs according to claim 3 or 4 prepare the high performance active carbon rich in micropore, feature
It is:The concentration of lye is with OH-Concentration is calculated as 0.2-2mol/L.
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Cited By (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN111003710A (en) * | 2020-01-17 | 2020-04-14 | 宿州学院 | Method for preparing nitrogen-doped graded porous carbon by using waste medicine residues and application of method |
CN111362265A (en) * | 2020-02-15 | 2020-07-03 | 太原理工大学 | VOCs adsorbent prepared from hypha solid waste resources and coal and preparation method thereof |
CN112142050A (en) * | 2020-09-29 | 2020-12-29 | 上海应用技术大学 | Method for preparing active coke by adopting antibiotic bacterium residue composite anthracite |
CN113413876A (en) * | 2021-08-05 | 2021-09-21 | 河南省高新技术实业有限公司 | Method for recycling antibiotic fungi residues |
CN113562730A (en) * | 2021-03-11 | 2021-10-29 | 海南师范大学 | Preparation of microporous gram bacteria carbon material with high specific surface area and application of microporous gram bacteria carbon material in supercapacitor |
CN114212791A (en) * | 2022-01-06 | 2022-03-22 | 华东理工大学 | Comprehensive treatment method for recycling antibiotic fungi residues |
CN114213479A (en) * | 2022-01-05 | 2022-03-22 | 山东润德生物科技有限公司 | Preparation method of glucosamine |
CN114684974A (en) * | 2022-04-22 | 2022-07-01 | 北京交通大学 | Source separation urine treatment system and method |
Citations (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102502630A (en) * | 2011-11-30 | 2012-06-20 | 河北科技大学 | Method for preparing activated carbon from penicillin or terramycin strain residues |
CN102847432A (en) * | 2012-09-24 | 2013-01-02 | 河北科技大学 | Method for adsorption-catalytic oxidation of sulfur dioxide by using metal modified antibiotic bacterium residue activated carbon |
CN103923734A (en) * | 2014-05-04 | 2014-07-16 | 天津理工大学 | Method for regenerating used oil by adopting antibiotic waste mushroom dreg biomass charcoal |
CN104998628A (en) * | 2015-07-21 | 2015-10-28 | 河北科技大学 | Bacterial residue active carbon supported TiO2 composite photocatalyst and applications thereof |
CN105819442A (en) * | 2016-03-23 | 2016-08-03 | 河北科技大学 | Method for preparing activated carbon by means of denitrification of waste penicillin mycelia |
CN105948041A (en) * | 2016-04-28 | 2016-09-21 | 深圳大学 | Fungus-based activated carbon nanofiber, and preparation method and application thereof |
CN106629708A (en) * | 2016-09-19 | 2017-05-10 | 北京化工大学 | Preparation method for waste edible-mushroom culture medium formed active carbon |
-
2018
- 2018-02-11 CN CN201810140010.3A patent/CN108455598A/en active Pending
Patent Citations (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102502630A (en) * | 2011-11-30 | 2012-06-20 | 河北科技大学 | Method for preparing activated carbon from penicillin or terramycin strain residues |
CN102847432A (en) * | 2012-09-24 | 2013-01-02 | 河北科技大学 | Method for adsorption-catalytic oxidation of sulfur dioxide by using metal modified antibiotic bacterium residue activated carbon |
CN103923734A (en) * | 2014-05-04 | 2014-07-16 | 天津理工大学 | Method for regenerating used oil by adopting antibiotic waste mushroom dreg biomass charcoal |
CN104998628A (en) * | 2015-07-21 | 2015-10-28 | 河北科技大学 | Bacterial residue active carbon supported TiO2 composite photocatalyst and applications thereof |
CN105819442A (en) * | 2016-03-23 | 2016-08-03 | 河北科技大学 | Method for preparing activated carbon by means of denitrification of waste penicillin mycelia |
CN105948041A (en) * | 2016-04-28 | 2016-09-21 | 深圳大学 | Fungus-based activated carbon nanofiber, and preparation method and application thereof |
CN106629708A (en) * | 2016-09-19 | 2017-05-10 | 北京化工大学 | Preparation method for waste edible-mushroom culture medium formed active carbon |
Cited By (10)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN111003710A (en) * | 2020-01-17 | 2020-04-14 | 宿州学院 | Method for preparing nitrogen-doped graded porous carbon by using waste medicine residues and application of method |
CN111362265A (en) * | 2020-02-15 | 2020-07-03 | 太原理工大学 | VOCs adsorbent prepared from hypha solid waste resources and coal and preparation method thereof |
CN111362265B (en) * | 2020-02-15 | 2022-02-25 | 太原理工大学 | VOCs adsorbent prepared from hypha solid waste resources and coal and preparation method thereof |
CN112142050A (en) * | 2020-09-29 | 2020-12-29 | 上海应用技术大学 | Method for preparing active coke by adopting antibiotic bacterium residue composite anthracite |
CN113562730A (en) * | 2021-03-11 | 2021-10-29 | 海南师范大学 | Preparation of microporous gram bacteria carbon material with high specific surface area and application of microporous gram bacteria carbon material in supercapacitor |
CN113413876A (en) * | 2021-08-05 | 2021-09-21 | 河南省高新技术实业有限公司 | Method for recycling antibiotic fungi residues |
CN114213479A (en) * | 2022-01-05 | 2022-03-22 | 山东润德生物科技有限公司 | Preparation method of glucosamine |
CN114212791A (en) * | 2022-01-06 | 2022-03-22 | 华东理工大学 | Comprehensive treatment method for recycling antibiotic fungi residues |
CN114684974A (en) * | 2022-04-22 | 2022-07-01 | 北京交通大学 | Source separation urine treatment system and method |
CN114684974B (en) * | 2022-04-22 | 2023-08-11 | 北京交通大学 | Source separation urine treatment system and method |
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