CN1648040A - Method for directly preparing honeycomb active carbon from coal - Google Patents
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- CN1648040A CN1648040A CN 200410092429 CN200410092429A CN1648040A CN 1648040 A CN1648040 A CN 1648040A CN 200410092429 CN200410092429 CN 200410092429 CN 200410092429 A CN200410092429 A CN 200410092429A CN 1648040 A CN1648040 A CN 1648040A
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Abstract
In the preparation of honeycomb active carbon directly with coal, coal powder, emulsified coal tar, water soluble adhesive, lubricant and water are produced into honeycomb active carbon through crushing, compounding, kneading, extruding, drying, carbonizing and activating. The present invention has low cost and simple production apparatus, and the prepared honeycomb active carbon has great specific surface area, high porosity, high resistance to water, acid and alkali, high compression strength, high heat resistance, and easy heat or washing regeneration.
Description
Technical field
The invention belongs to a kind of manufacture method of Alveolate activated carbon capable, relate in particular to a kind of method that directly prepares Alveolate activated carbon capable by coal.
Background technology
China is coal-fired big country, and coal accounts for 75% of primary energy source total quantity consumed.Along with the continuous growth of consumption of coal, coal fire discharged sulfurous gas, oxynitride also constantly increase, and surpass 2000 and 9,100,000 tons for years, occupy first place in the world, cause China's acid rain and sulfur dioxide pollution to be on the rise.According to the estimation of relevant research, by 2000 and 2010, the NOx quantity discharged of China will reach 1,561 ten thousand tons and 2,194 ten thousand tons respectively.China has begun to mention agenda to the NOx discharging and the control of polluting, and clearly proposes in " the atmosphere method " of nineteen ninety-five revision " oxynitride that enterprise should progressively produce fire coal take control measure ".Therefore, strengthen the research of oxynitride control techniques in the fire coal boiler fume, exploitation is fit to the control techniques of China's national situation, and strengthen environmental protection work is the important assurance that China implements the strategy of sustainable development.
Honeycombed catalyst has the advantages that geometrical surface is big, voidage is high, bed pressure drop is low, and therefore, the preparation of honeycombed catalyst and utilisation technology become in recent years scientific worker's research focus both at home and abroad.At present, main two classes of Alveolate activated carbon capable technology of preparing of patent documentation report: the method for forming and dip coating.U.S.Pat.No.3,825,460 reports use the papery honeycomb to be parent, by dip-coating powdered carbon (as carbon black, natural or graphous graphite powder, coke powder, coal dust) or sugar, phenol-formaldehyde resin powder, cacao shell powder, walnut parting and solution, suspension or emulsion natural or staple fibre and organic bond (as coal-tar pitch, resol, Resins, epoxy) configuration, through 110 ℃ of dryings, 600-1000 ℃ inert atmosphere charing, 700-1000 ℃ of activation obtains specific surface area 300-800m
2/ g Alveolate activated carbon capable.U.S.Pat.No.4; 399; 052 employing phenol-formaldehyde resin powder, powdered carbon are activated carbon precursor, and silicon carbide, titanium carbide are toughener, and carboxymethyl cellulose is the temporary adhesion agent; water soluble phenol resin is a binding agent; material is by mixing, kneading, extrusion moulding, then under the argon shield condition in 750 ℃ of charings 5 hours, 900-950 ℃ steam activation 3-5 hour; the Alveolate activated carbon capable malleation intensity 6.5-8.25Mpa, the side pressure strength 0.8-2.8Mpa that make, specific surface area 920-1120m
2/ g, heat shock resistance 400-900 ℃.U.S.Pat.No.4,992,319 use the glass fibre corrugation paper of high voidage to be parent, the suspension that dip-coating gac and vinylformic acid or vinylidene resin are made, and the Alveolate activated carbon capable that obtains after the drying can be used for filtering ozone, foul smell and support of the catalyst.U.S.Pat.No.5; 356; 852, E.P.Pat.No.492081A1 adopts multipolymer, the silicone resin of activity charcoal powder and Vltra tears, polyvinyl alcohol or polyvinyl alcohol and poly-ethylene methacrylic ester to add water or ethanol to make and plastify mud cream; pass through extrusion moulding then, 100 ℃ or 200 ℃ of (carbon-dioxide protecting) dryings make ultimate compression strength 1.13-6.88Mpa, specific surface area 646-1300m
2/ g.E.P.Pat.No.728, the 521B1 report uses resol to be activated carbon precursor, Mierocrystalline cellulose, kaolin, trichroite are filler, MC or cellulose ester are temporary transient tamanori, soap or linolic acid are lubricant, add suitable quantity of water and be mixed with plastic mud material, honeycomb steel die hole density is 16-32 hole/cm
2The time extrusion pressure between 3.7-7.6Mpa, honeycomb solidifies 3 hours, 900 ℃ charings 5 hours, 800-900 ℃ carbonic acid gas activation 1 hour, the Alveolate activated carbon capable benzene adsorptive capacity 213-601mg/g that makes at 150 ℃.U.S.Pat.No.6,284,705B1, U.S.Pat.No.6,171,373B1 has reported a kind of method of utilizing gac and mineral binder bond to prepare Alveolate activated carbon capable.Specific surface area 600-2000m
2The 50-30 in proportion of the gac of/g and mineral binder bond: 50-70 configuration, mineral binder bond is suitably allocated by clay, kaolin, nepheline and water glass and is formed.Mentioned component additionally adds the methylcellulose gum of 2.5-3% again and the water of 66-102% is made plasticity mud cream, and the extrusion moulding honeycomb is through freezing or vacuum-drying, inert atmosphere protection high-temperature calcination, and ultimate compression strength can reach 1.4-8.9Mpa.U.S.Pat.No.6,699,561B2 proposed another kind of direct usefulness 34 ~ 37% activity charcoal powders and 11-12% phenol-formaldehyde resin powder, 5-10% clay, 2-3% cellulose ester, 7-8% starch paste, 0.5-0.9% polyacrylamide, 4-5% paraffin, 1.5-1.7% soap, 27-31% water through mixing, extrude, shaping, drying and 650-850 ℃ charing 5-30 minute, the cellular activated carbon that obtains can be used as adsorption filter, and available electrically heated regeneration.In sum, in order to improve the ultimate compression strength of Alveolate activated carbon capable, a kind of way is to adopt mineral binder bond to realize in high-temperature calcination, and another kind of way is to utilize resin that can charing and add the carbide toughener and realize.Must cause the effectively reduction of carbon content in the honeycomb like this, and the production cost increase, be difficult to industrialization promotion and use.
Summary of the invention
What the purpose of this invention is to provide that a kind of production cost is low, ultimate compression strength is high directly prepares the method for Alveolate activated carbon capable by coal
The preparation method of Alveolate activated carbon capable of the present invention is obtained through raw material pulverizing, batching, kneading, extrusion moulding, drying, charing, activation by coal dust, emulsification coal tar, water-soluble binder, lubricant and water.Concrete preparation method may further comprise the steps:
(1) coal dust configuration: brown coal or bituminous coal and coking coal are crushed to respectively≤2mm, then by quality than brown coal or bituminous coal: after coking coal=1: the 0.2-0.5 mixing, be ground to below the 74 μ m coal dust that obtains mixing again;
(2) emulsification coal tar: the first step, asphalt content 〉=55% coal-tar heavy oil is preheated to 120-150 ℃; Second step, the preparation of emulsifier aqueous solution, the stablizer of the 0.5-2% of the 2-6% tensio-active agent of adding coal-tar heavy oil quality and coal-tar heavy oil quality in water, and be preheated to 80-90 ℃ of formation emulsifier aqueous solution; The 3rd step was a coal-tar heavy oil by mass ratio: emulsifier aqueous solution=1: 0.3-0.7 under agitation condition, adds coal-tar heavy oil and makes emulsification coal tar in the emulsifier aqueous solution;
(3) processing of plasticity-coal slime: by mass ratio is coal dust: emulsification coal tar: water: water-soluble binder: lubricant=34-57: 30-36: 6-29: 3-5: 2-3, with stirring in its adding kneader, make plastic coal slime;
(4) pugging: the plasticity-coal slime is handled through vacuum deairing machine or extrusion shaping machine, and coal slime is mixed, and removes large particulate matter with 60 to 100 purpose silk screen filter then in shaper;
(5) extrusion moulding: the coal slime adding after pugging is handled is equipped with in the extrusion shaping machine of honeycomb steel die, carries out moulding, the honeycomb that obtains wetting;
(6) drying: wet honeycomb is dried to moisture and is lower than 2%;
(7) charing and activation: as protection gas, be heated to 600-800 ℃ with rare gas element by heat-up rate 3-5 ℃/min, and under this temperature charing 2-3 hour; Be warmed up to 750-850 ℃ by heat-up rate 5-15 ℃/min then, use steam activation 3-15 hour, obtain Alveolate activated carbon capable.
Aforesaid tensio-active agent is sodium lignosulfonate, humate, sodium formaldehyde condensation products or polymethylene anthracene sulfonic acid sodium.
Aforesaid stablizer can be selected divalence or trivalent soluble metallic salt, as calcium chloride, ferric sulfate or iron nitrate etc.
Aforesaid water-soluble binder is to select starch, polyvinyl alcohol (PVA), cellulose ester (comprising methylcellulose gum, ethyl cellulose, Vltra tears), Natvosol and Xylo-Mucine (CMC) etc.
Aforesaid lubricant can be the saponification material that tung oil, oleum lini or edible oil and production process thereof produce.
Aforesaid steel die can adopt 8-16 hole/cm
2Square hole honeycomb steel die
Aforesaid forming pressure is 7-14Mpa.
Aforesaid rare gas element is nitrogen or argon gas.
The Alveolate activated carbon capable of the present invention's preparation is specially adapted to the purification of fire coal, oil-firing boiler tail gas clean-up and the indoor harmful gas of electric power, chemical fertilizer, metallurgy industry, technical fields such as Treatment of Industrial Water, support of the catalyst.
Compared with the prior art the present invention has the following advantages:
(1) be that the Alveolate activated carbon capable cost made of activated carbon precursor is extremely low with cheap bituminous coal or brown coal;
(2) use coal-tar heavy oil as binding agent, and carried out emulsification, kneading, moulding process can be finished at normal temperatures, make kneading, extrusion not need the insulation measure, production unit is simplified greatly.
(3) absorption of Alveolate activated carbon capable, catalytic performance and physical property (as geometrical shape, size, pore size distribution, intensity etc.) can be carried out cutting as required.
(4) this Alveolate activated carbon capable has the advantages that the unit volume specific surface area is big, voidage is high, bed pressure drop is low, can prevent the latch up phenomenon that particulate matter causes in dust or the water.
(5) the water-fast acid-fast alkali-proof of this Alveolate activated carbon capable, ultimate compression strength height, good heat resistance, heat regeneration or regenerated from washing easily.
Embodiment
Embodiment 1:
(1) coal dust configuration: brown coal and coking coal are crushed to respectively≤2mm, then by quality than brown coal: after coking coal=mixing in 1: 0.3, be ground to below the 74 μ m coal dust that obtains mixing again.
(2) emulsification coal tar: the first step, asphalt content are that 57% coal-tar heavy oil is preheated to 120 ℃; Second step, the preparation emulsifier aqueous solution.Add 4% tensio-active agent (is benchmark with coal tar) and 0.5% stablizer (is benchmark with coal tar) in the water, and be preheated to 80 ℃ and form emulsifier aqueous solutions; In the 3rd step, press coal-tar heavy oil: emulsifier aqueous solution (mass ratio)=1: 0.5 slowly adds coal tar under agitation condition and makes emulsification coal tar in the emulsifier aqueous solution.The tensio-active agent of emulsification coal-tar heavy oil is a sodium lignosulfonate, and stablizer is a calcium chloride.
(3) processing of plasticity-coal slime: coal dust in proportion: emulsification coal tar: water: polyvinyl alcohol: tung oil=38: 36: 20: add in kneaders at 4: 2 and to stir, make plastic coal slime.
(4) pugging: the plasticity-coal slime is handled through vacuum deairing machine or extrusion shaping machine, and coal slime is mixed, and removes the large particulate matter that above-mentioned operation may be brought into 60 purpose silk screen filter then in shaper.
(5) extrusion moulding: the coal slime adding after pugging is handled is equipped with in the extrusion shaping machine of honeycomb steel die, is to carry out moulding, the honeycomb that obtains wetting under the 7Mpa in forming pressure.
(6) drying: wet honeycomb is dried to moisture and is lower than 2%.
(7) charing and activation: as protection gas, be heated to 600 ℃ with nitrogen or argon gas by 3 ℃/min of heat-up rate, and charing 2 hours under this temperature; Being warmed up to 800 ℃ by 5 ℃/min of heat-up rate then, is activated media activation 3 hours with water vapour, obtains Alveolate activated carbon capable.The cellular activated carbon performance index see Table 1
Embodiment 2:
(1) coal dust configuration: brown coal and coking coal are crushed to respectively≤2mm, then by quality than brown coal: after coking coal=mixing in 1: 0.2, be ground to below the 74 μ m coal dust that obtains mixing again.
(2) emulsification coal tar: the first step, asphalt content be 58% be preheated to 140 ℃ from warm coal tar; Second step, the preparation emulsifier aqueous solution.Add 5% tensio-active agent (is benchmark with coal tar) and 2% stablizer (is benchmark with coal tar) in the water, and be preheated to 85 ℃ and form emulsifier aqueous solutions; In the 3rd step, press coal-tar heavy oil: emulsifier aqueous solution (mass ratio)=1: 0.6 slowly adds coal tar under agitation condition and makes emulsification coal tar in the emulsifier aqueous solution.The tensio-active agent of emulsification coal-tar heavy oil is a humate, and stablizer is a ferric sulfate.
(3) processing of plasticity-coal slime: coal dust in proportion: emulsification coal tar: water: W-Gum: oleum lini=40: 30: 25: add in kneaders at 5: 3 and to stir, make plastic coal slime.
(4) pugging: the plasticity-coal slime is handled through vacuum deairing machine or extrusion shaping machine, and coal slime is mixed, and removes the large particulate matter that above-mentioned operation may be brought into 80 purpose silk screen filter then in shaper.
(5) extrusion moulding: the coal slime adding after pugging is handled is equipped with in the extrusion shaping machine of honeycomb steel die, is to carry out moulding, the honeycomb that obtains wetting under the 7Mpa in forming pressure.
(6) drying: the honeycomb of extruding is dried to moisture and is lower than 2%.
(7) charing and activation: as protection gas, be heated to 700 ℃ with nitrogen or argon gas, and under this temperature, be incubated 3 hours by 5 ℃/min of heat-up rate; Being warmed up to 800 ℃ by 10 ℃/min of heat-up rate then, is activated media activation 5 hours with water vapour, obtains Alveolate activated carbon capable.The cellular activated carbon performance index see Table 1
Embodiment 3:
(1) coal dust configuration: bituminous coal and coking coal are crushed to respectively≤2mm, then by quality than bituminous coal: after coking coal=mixing in 1: 0.5, be ground to below the 74 μ m coal dust that obtains mixing again.
(2) emulsification coal tar: the first step, asphalt content are that 55% coal-tar heavy oil is preheated to 140 ℃; Second step, the preparation emulsifier aqueous solution.Add in stablizer (is benchmark with the coal tar) water of 2% tensio-active agent (is benchmark with coal tar) and 0.5%, and be preheated to 85 ℃ and form emulsifier aqueous solutions; In the 3rd step, press coal-tar heavy oil: emulsifier aqueous solution (mass ratio)=1: 0.3 slowly adds coal tar under agitation condition and makes emulsification coal tar in the emulsifier aqueous solution.The tensio-active agent of emulsification coal-tar heavy oil is the sodium formaldehyde condensation products, and stablizer is a ferric sulfate.
(3) processing of plasticity-coal slime: coal dust in proportion: emulsification coal tar: water: methylcellulose gum: tung oil oil=57: 30: 8: add in kneaders at 3: 2 and to stir, make plastic coal slime.
(4) pugging: the plasticity-coal slime is handled through vacuum deairing machine or extrusion shaping machine, and coal slime is mixed, and removes the large particulate matter that above-mentioned operation may be brought into 80 purpose silk screen filter then in shaper.
(5) extrusion moulding: the coal slime adding after pugging is handled is equipped with in the extrusion shaping machine of honeycomb steel die, is to carry out moulding, the honeycomb that obtains wetting under the 14Mpa in forming pressure.
(6) drying: wet honeycomb is dried to moisture and is lower than 2%.
(7) charing and activation: as protection gas, be heated to 800 ℃ with nitrogen or argon gas by 3 ℃/min of heat-up rate, and charing 2 hours under this temperature; Being warmed up to 750 ℃ by 10 ℃/min of heat-up rate then, is activated media activation 15 hours with water vapour, obtains Alveolate activated carbon capable.The cellular activated carbon performance index see Table 1
Embodiment 4:
(1) coal dust configuration: bituminous coal and coking coal are crushed to respectively≤2mm, then by quality than bituminous coal: after coking coal=mixing in 1: 0.4, be ground to below the 74 μ m coal dust that obtains mixing again.
(2) emulsification coal tar: the first step, asphalt content are that 56% coal-tar heavy oil is preheated to 140 ℃; Second step, the preparation emulsifier aqueous solution.Add 4% tensio-active agent (is benchmark with coal tar) and 1% stablizer (is benchmark with coal tar) in the water, and be preheated to 85 ℃ and form emulsifier aqueous solutions; In the 3rd step, press coal-tar heavy oil: emulsifier aqueous solution (mass ratio)=1: 0.3 slowly adds coal tar under agitation condition and makes emulsification coal tar in the emulsifier aqueous solution.The tensio-active agent of emulsification coal-tar heavy oil is the sodium formaldehyde condensation products, and stablizer is a calcium chloride.
(3) processing of plasticity-coal slime: coal dust in proportion: emulsification coal tar: water: ethyl cellulose: soya-bean oil=50: 30: 13: add in kneaders at 4: 3 and to stir, make plastic coal slime.
(4) pugging: the plasticity-coal slime is handled through vacuum deairing machine or extrusion shaping machine, and coal slime is mixed, and removes the large particulate matter that above-mentioned operation may be brought into 80 purpose silk screen filter then in shaper.
(5) extrusion moulding: the coal slime adding after pugging is handled is equipped with in the extrusion shaping machine of honeycomb steel die, is to carry out moulding, the honeycomb that obtains wetting under the 12Mpa in forming pressure.
(6) drying: wet honeycomb is dried to moisture and is lower than 2%.
(7) charing and activation: as protection gas, be heated to 700 ℃ with nitrogen or argon gas by 3 ℃/min of heat-up rate, and charing 2 hours under this temperature; Being warmed up to 800 ℃ by 10 ℃/min of heat-up rate then, is activated media activation 10 hours with water vapour, obtains Alveolate activated carbon capable.The cellular activated carbon performance index see Table 1
Embodiment 5:
(1) coal dust configuration: bituminous coal and coking coal are crushed to respectively≤2mm, then by quality than bituminous coal: after coking coal=mixing in 1: 0.3, be ground to below the 74 μ m coal dust that obtains mixing again.
(2) emulsification coal tar: the first step, asphalt content are that 56% coal-tar heavy oil is preheated to 140 ℃; Second step, the preparation emulsifier aqueous solution.Add 5% tensio-active agent (is benchmark with coal tar) and 0.5% stablizer (is benchmark with coal tar) in the water, and be preheated to 85 ℃ and form emulsifier aqueous solutions; In the 3rd step, press coal-tar heavy oil: emulsifier aqueous solution (mass ratio)=1: 0.5 slowly adds coal tar under agitation condition and makes emulsification coal tar in the emulsifier aqueous solution.The tensio-active agent of emulsification coal-tar heavy oil is a polymethylene anthracene sulfonic acid sodium, and stablizer is an iron nitrate.
(3) processing of plasticity-coal slime: coal dust in proportion: emulsification coal tar: water: Vltra tears: soya-bean oil saponification material=45: 33: 15: add in kneaders at 5: 2 and to stir, make plastic coal slime.
(4) pugging: the plasticity-coal slime is handled through vacuum deairing machine or extrusion shaping machine, and coal slime is mixed, and removes the large particulate matter that above-mentioned operation may be brought into 100 purpose silk screen filter then in shaper.
(5) extrusion moulding: the coal slime adding after pugging is handled is equipped with in the extrusion shaping machine of honeycomb steel die, is to carry out moulding, the honeycomb that obtains wetting under the 10Mpa in forming pressure.
(6) drying: wet honeycomb is dried to moisture and is lower than 2%.
(7) charing and activation: as protection gas, be heated to 600 ℃ with nitrogen or argon gas by 4 ℃/min of heat-up rate, and charing 2 hours under this temperature; Being warmed up to 800 ℃ by 10 ℃/min of heat-up rate then, is activated media activation 8 hours with water vapour, obtains Alveolate activated carbon capable.The cellular activated carbon performance index see Table 1
Embodiment 6:
(1) coal dust configuration: bituminous coal and coking coal are crushed to respectively≤2mm, then by quality than bituminous coal: after coking coal=mixing in 1: 0.2, be ground to below the 74 μ m coal dust that obtains mixing again.
(2) emulsification coal tar: the first step, asphalt content are that 60% coal-tar heavy oil is preheated to 140 ℃; Second step, the preparation emulsifier aqueous solution.Add 6% tensio-active agent (is benchmark with coal tar) and 2% stablizer (is benchmark with coal tar) in the water, and be preheated to 85 ℃ and form emulsifier aqueous solutions; In the 3rd step, press coal-tar heavy oil: emulsifier aqueous solution (mass ratio)=1: 0.7 slowly adds coal tar under agitation condition and makes emulsification coal tar in the emulsifier aqueous solution.The tensio-active agent of emulsification coal-tar heavy oil is a polymethylene anthracene sulfonic acid sodium, and stablizer is an iron nitrate.
(3) processing of plasticity-coal slime: coal dust in proportion: emulsification coal tar: water: Natvosol: tung oil oil=34: 36: 22: add in kneaders at 5: 3 and to stir, make plastic coal slime.
(4) pugging: the plasticity-coal slime is handled through vacuum deairing machine or extrusion shaping machine, and coal slime is mixed, and removes the large particulate matter that above-mentioned operation may be brought into 60 purpose silk screen filter then in shaper.
(5) extrusion moulding: the coal slime adding after pugging is handled is equipped with in the extrusion shaping machine of honeycomb steel die, is to carry out moulding, the honeycomb that obtains wetting under the 7Mpa in forming pressure.
(6) drying: wet honeycomb is dried to moisture and is lower than 2%.
(7) charing and activation: as protection gas, be heated to 700 ℃ with nitrogen or argon gas by 3 ℃/min of heat-up rate, and charing 2 hours under this temperature; Being warmed up to 850 ℃ by 15 ℃/min of heat-up rate then, is activated media activation 6 hours with water vapour, obtains Alveolate activated carbon capable.The cellular activated carbon performance index see Table 1
Embodiment 7:
(1) coal dust configuration: bituminous coal and coking coal are crushed to respectively≤2mm, then by quality than bituminous coal: after coking coal=mixing in 1: 0.2, be ground to below the 74 μ m coal dust that obtains mixing again.
(2) emulsification coal tar: the first step, asphalt content are that 60% coal-tar heavy oil is preheated to 140 ℃; Second step, the preparation emulsifier aqueous solution.Add 6% tensio-active agent (is benchmark with coal tar) and 2% stablizer (is benchmark with coal tar) in the water, and be preheated to 85 ℃ and form emulsifier aqueous solutions; In the 3rd step, press coal-tar heavy oil: emulsifier aqueous solution (mass ratio)=1: 0.7 slowly adds coal tar under agitation condition and makes emulsification coal tar in the emulsifier aqueous solution.The tensio-active agent of emulsification coal-tar heavy oil is a polymethylene anthracene sulfonic acid sodium, and stablizer is an iron nitrate.
(3) processing of plasticity-coal slime: coal dust in proportion: emulsification coal tar: water: Xylo-Mucine: tung oil=34: 36: 22: add in kneaders at 5: 3 and to stir, make plastic coal slime.
(4) pugging: the plasticity-coal slime is handled through vacuum deairing machine or extrusion shaping machine, and coal slime is mixed, and removes the large particulate matter that above-mentioned operation may be brought into 60 purpose silk screen filter then in shaper.
(5) extrusion moulding: the coal slime adding after pugging is handled is equipped with in the extrusion shaping machine of honeycomb steel die, is to carry out moulding, the honeycomb that obtains wetting under the 7Mpa in forming pressure.
(6) drying: wet honeycomb is dried to moisture and is lower than 2%.
(7) charing and activation: as protection gas, be heated to 650 ℃ with nitrogen or argon gas by 5 ℃/min of heat-up rate, and charing 2 hours under this temperature; Being warmed up to 850 ℃ by 15 ℃/min of heat-up rate then, is activated media activation 3 hours with water vapour, obtains Alveolate activated carbon capable.The cellular activated carbon performance index see Table 1
Table 1 cellular activated carbon performance index table look-up
| Performance | Embodiment 1 | Embodiment 2 | Embodiment 3 | Embodiment 4 | Embodiment 5 | Embodiment 6 | Embodiment 7 |
| Specific surface area, m 2/g | ?284 | ?235 | ?1040 | ?812 | ?412 | ?578 | ?286 |
| Pore volume, ml/g | ?0.31 | ?0.42 | ?0.86 | ?0.63 | ?0.56 | ?0.57 | ?0.34 |
| Ultimate compression strength, Mpa | ?13 | ?3 | ?16 | ?24 | ?2 | ?29 | ?36 |
| Point of ignition, ℃ | ?400 | ?450 | ?500 | ?500 | ?480 | ?450 | ?400 |
Claims (10)
1, a kind ofly directly prepares the method for Alveolate activated carbon capable, it is characterized in that comprising the steps: by coal
(1) coal dust configuration: brown coal or bituminous coal and coking coal are crushed to respectively≤2mm, then by quality than brown coal or bituminous coal: after coking coal=1: the 0.2-0.5 mixing, be ground to below the 74 μ m coal dust that obtains mixing again;
(2) emulsification coal tar: the first step, asphalt content 〉=55% coal-tar heavy oil is preheated to 120-150 ℃; Second step, the preparation of emulsifier aqueous solution, the stablizer of the 0.5-2% of the 2-6% tensio-active agent of adding coal-tar heavy oil quality and coal-tar heavy oil quality in water, and be preheated to 80-90 ℃ of formation emulsifier aqueous solution; The 3rd step was a coal-tar heavy oil by mass ratio: emulsifier aqueous solution=1: 0.3-0.7 under agitation condition, adds coal-tar heavy oil and makes emulsification coal tar in the emulsifier aqueous solution;
(3) processing of plasticity-coal slime: by mass ratio is coal dust: emulsification coal tar: water: water-soluble binder: lubricant=34-57: 30-36: 6-29: 3-5: 2-3, with stirring in its adding kneader, make plastic coal slime;
(4) pugging: the plasticity-coal slime is handled through vacuum deairing machine or extrusion shaping machine, and coal slime is mixed, and removes large particulate matter with 60 to 100 purpose silk screen filter then in shaper;
(5) extrusion moulding: the coal slime adding after pugging is handled is equipped with in the extrusion shaping machine of honeycomb steel die, carries out moulding, the honeycomb that obtains wetting;
(6) drying: wet honeycomb is dried to moisture and is lower than 2%;
(7) charing and activation: as protection gas, be heated to 600-800 ℃ with rare gas element by heat-up rate 3-5 ℃/min, and under this temperature charing 2-3 hour; Be warmed up to 750-850 ℃ by heat-up rate 5-15 ℃/min then, use steam activation 3-15 hour, obtain Alveolate activated carbon capable.
2, as claimed in claim 1ly a kind ofly directly prepare the method for Alveolate activated carbon capable, it is characterized in that described tensio-active agent is sodium lignosulfonate, humate, sodium formaldehyde condensation products or polymethylene anthracene sulfonic acid sodium by coal.
3, as claimed in claim 1ly a kind ofly directly prepare the method for Alveolate activated carbon capable, it is characterized in that described stablizer selects divalence or trivalent soluble metallic salt by coal.
4, as claimed in claim 3ly a kind ofly directly prepare the method for Alveolate activated carbon capable, it is characterized in that described divalence or trivalent soluble metallic salt are calcium chloride, ferric sulfate or iron nitrate by coal.
5, as claimed in claim 1ly a kind ofly directly prepare the method for Alveolate activated carbon capable, it is characterized in that described water-soluble binder is starch, polyvinyl alcohol, cellulose ester, Natvosol or Xylo-Mucine by coal.
6, as claimed in claim 5ly a kind ofly directly prepare the method for Alveolate activated carbon capable, it is characterized in that described cellulose ester is methylcellulose gum, ethyl cellulose or Vltra tears by coal.
7, as claimed in claim 1ly a kind ofly directly prepare the method for Alveolate activated carbon capable, it is characterized in that described lubricant is the saponification material that tung oil, oleum lini or edible oil and production process thereof produce by coal.
8, as claimed in claim 1ly a kind ofly directly prepare the method for Alveolate activated carbon capable, it is characterized in that described steel die adopts 8-16 hole/cm by coal
2Square hole honeycomb steel die.
9, as claimed in claim 1ly a kind ofly directly prepare the method for Alveolate activated carbon capable, it is characterized in that described forming pressure is 7-14Mpa by coal.
10, as claimed in claim 1ly a kind ofly directly prepare the method for Alveolate activated carbon capable, it is characterized in that described rare gas element is nitrogen or argon gas by coal.
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 200410092429 CN1288077C (en) | 2004-12-21 | 2004-12-21 | Method for directly preparing honeycomb active carbon from coal |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 200410092429 CN1288077C (en) | 2004-12-21 | 2004-12-21 | Method for directly preparing honeycomb active carbon from coal |
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| CN1648040A true CN1648040A (en) | 2005-08-03 |
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| CN101857224A (en) * | 2010-06-11 | 2010-10-13 | 清华大学 | Preparation method of phenolic resin combined honeycomb activated carbon |
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| CN101766991A (en) * | 2010-02-11 | 2010-07-07 | 赵建勋 | Unshaped activated coke adsorption catalyst |
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| CN101766991B (en) * | 2010-02-11 | 2012-06-13 | 赵建勋 | Unshaped activated coke adsorption catalyst |
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| CN114752349A (en) * | 2022-04-18 | 2022-07-15 | 宁夏西泰煤化工有限公司 | Coal-based activated carbon binder based on high-temperature coal tar and modified asphalt, and production method and system thereof |
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