CN101342480A - Tetroxide tetrsilver coal absorbent charcoal, preparation method and uses thereof - Google Patents
Tetroxide tetrsilver coal absorbent charcoal, preparation method and uses thereof Download PDFInfo
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- CN101342480A CN101342480A CNA2008100219066A CN200810021906A CN101342480A CN 101342480 A CN101342480 A CN 101342480A CN A2008100219066 A CNA2008100219066 A CN A2008100219066A CN 200810021906 A CN200810021906 A CN 200810021906A CN 101342480 A CN101342480 A CN 101342480A
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- coal
- tetroxide
- tetrsilver
- active carbon
- absorbent charcoal
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Abstract
The invention has discloses a tetrasilver tetroxide coal activated carbon, a preparation method and an application; the tetrasilver tetroxide coal activated carbon contains coal activated carbon and tetrasilver tetroxide; the tetrasilver tetroxide is adsorbed on the surface or the aperture of the coal activated carbon. The preparation method is as follows: the coal activated carbon is washed and dried for stand-by; the tetrasilver tetroxide is blended with an alkalescent solvent; the blended liquid is sprayed on the coal activated carbon; a silver-loaded coal activated carbon is re-dried so as to obtain the tetrasilver tetroxide coal activated carbon. As a filter material, the tetrasilver tetroxide coal activated carbon is applied in a water cleaner and a direct drinking water supply project. The silver on the surface of the tetrasilver tetroxide coal activated carbon prepared by the preparation method cannot fall off; the tetrasilver tetroxide coal activated carbon can be applied to the water cleaner and other direct drinking water projects to effectively adsorb and kill bacteria and a hazardous substance and produce drinking water which is clean and useful for human health and meets a hygienic standard of people.
Description
Technical field
The present invention relates to a kind of tetroxide tetrsilver coal absorbent charcoal, preparation method and as the application of filtering material.
Background technology
At present, filtering material miscellaneous is a lot of on the domestic market, its purposes is respectively arranged with not enough.And active carbon is exactly one of them, the filter of doing the filtrate manufacturing with active carbon uses certain hour, because active carbon itself has only suction-operated, there is not the sterilization algae removal effect, through charcoal absorption behind the certain hour behind a large amount of organic pollutions, microorganism very easily breeds, organic matter decomposes on the interface of active carbon under action of microorganisms, make organic nitrogen progressively be decomposed into proteinic nitrogen, ammonia nitrogen, nitrite nitrogen, make that content of nitrite increases in the water outlet of active carbon filter, can be in active carbon and filter bed in endophytic bacteria etc. and produce secondary pollution now, so not only do not reach the purpose that purifies water, on the contrary can polluted water.In recent years along with the sterilizing mechanisms of silver is familiar with by people gradually, silver (or carrying silver) active carbon that oozes miscellaneous constantly appears in market, manufacture method mostly is the solution infusion method, there be coming off in various degree in silver, silver is a heavy metal species, be insalubrious, the problem of coming off that how to solve active carbon loading silver silver in water treatment is a difficult problem.
Summary of the invention
Goal of the invention: the object of the invention is to provide a kind of impurity, dirt, nuisance etc. of can adsorbing again can sterilization algae removal, simultaneously silver in water treatment procedure difficult drop-off, can directly apply to the tetroxide tetrsilver coal absorbent charcoal that drinking water filters.
Another object of the present invention is to provide a kind of preparation method of above-mentioned tetroxide tetrsilver coal absorbent charcoal.
Another object of the present invention is to provide the application of this tetroxide tetrsilver coal absorbent charcoal.
Technical scheme: a kind of tetroxide tetrsilver coal absorbent charcoal, it comprises coal mass active carbon and Tetrasilver tetroxide, described Tetrasilver tetroxide adsorbed close is in the aperture of the surface of coal mass active carbon or active carbon.
Tetrasilver tetroxide content in per 100 gram tetroxide tetrsilver coal absorbent charcoals is not less than 0.1 milligram.
Described coal mass active carbon is 9～11 orders.
The preparation method of above-mentioned tetroxide tetrsilver coal absorbent charcoal comprises the steps:
1), that coal mass active carbon cleaning and dry back is standby; Tetrasilver tetroxide and pH value are mixed by weight 0.5～1 ‰ ratio at 7.0～7.5 alkalescent solvent;
2), the mixed liquor in the step 1) is sprayed to temperature on 50～80 ℃ coal mass active carbon;
3) with step 2) in make carry silver-colored coal mass active carbon under 70～90 ℃, promptly obtained tetroxide tetrsilver coal absorbent charcoal in 8～15 minutes at sealing equipment inner drying against sunshine.
Alkalescent solvent described in the above-mentioned steps (1) is a kind of in ammoniacal liquor, sodium hydroxide solution, the aqua calcis.
Above-mentioned coal mass active carbon be 9～11 orders, quality meets the GB/T7702 standard.
Tetroxide tetrsilver coal absorbent charcoal is as the application of filtering material in water purifier and direct drinking water supply project equipment.
Tetroxide tetrsilver coal absorbent charcoal is the honeycomb that utilizes coal mass active carbon abundant, higher intensity, reasonable proportioning, Tetrasilver tetroxide is sprayed to the surface of coal mass active carbon, in certain temperature, under time, the free enthalpy of material increases, the molecule of physical absorption can absorb energy and excite the possibility that enters chemisorbed, in other words, because intermolecular energy excites, surface treated active carbon, its surface free radical group is active, combine closely with silver ion, material increases from the possibility that intermolecular combination carries out the transition to the covalent bonds form, thereby can not come off because of flowing water washes away, a kind ofly can adsorb and kill harmful substance thereby make, the tetroxide tetrsilver coal absorbent charcoal of bacterium.
Beneficial effect: tetroxide tetrsilver coal absorbent charcoal of the present invention can be removed chlorine residue, heavy metal, organic pollution effectively, has solved in the prior art and can only adsorb impurity, bacterium, and it can not have been killed and cause secondary pollution problem.The silver on the tetroxide tetrsilver coal absorbent charcoal surface that preparation method of the present invention makes can not come off, technology simple, can realize large-scale industrial production.Tetroxide tetrsilver coal absorbent charcoal is applied to the purification of water purifier or other direct drinking water projects, particularly in bottled water is produced, need not carry out ozonization in addition and handle and get final product long-period freshness preserving, and the water quality after handling is less scaling, mouthfeel is obviously improved; Water after the processing has kept the natural mineral matter to the human body beneficial; The water quality meta-alkalescence; Dissolved oxygen on average increases about 30%; Have long-acting inhibition bacterium, virus, the effect of algae meets the water standard of the healthy water that domestic and international expert generally acknowledges.
Description of drawings
Fig. 1 is the schematic diagram of absorbent charcoal cleaning machine.
Fig. 2 is the front view of Fig. 1.
Fig. 3 is the schematic diagram of drying machine.
Fig. 4 is the front view of Fig. 3.
The specific embodiment
Below in conjunction with embodiment the present invention is further described.
The invention discloses a kind of tetroxide tetrsilver coal absorbent charcoal, it comprises coal mass active carbon and Tetrasilver tetroxide (Ag
4O
4), described Tetrasilver tetroxide adsorbed close is in the aperture of the surface of coal mass active carbon or active carbon, Tetrasilver tetroxide content in per 100 gram tetroxide tetrsilver coal absorbent charcoals is not less than 0.1 milligram, described coal mass active carbon quality meets the GB/T7702 standard, selects 9～11 purpose coal mass active carbons for use.Active carbon has suction-operated, and silver has bactericidal action, the two is in conjunction with making the present invention can adsorb and kill harmful substance, Tetrasilver tetroxide content in guaranteeing per 100 gram tetroxide tetrsilver coal absorbent charcoals is not less than 0.1 milligram hour, all have absorption impurity, nuisance, and kill harmful bacterium etc.
Embodiment 1: 10 purpose coal mass active carbon 100kg cleaned in absorbent charcoal cleaning machine, and dry then; With 1 gram Ag
4O
4With 1000 gram pH values is that 7.2 aqueous ammonia solvent is diluted to solution, is ejected into by constant displacement pump and atomization jetting device on the coal mass active carbon that has 60 ℃ after the drying; To carry silver-colored coal mass active carbon then in the sealing of 80 ℃ of temperature drying machine against sunshine, by convection heat transfer' heat-transfer by convection, hot blast conduction, frequency control blower fan: 10Hz drying, last under 13 minutes time conditions, make the 100Kg tetroxide tetrsilver coal absorbent charcoal, contain the 0.8g Tetrasilver tetroxide in the 100Kg tetroxide tetrsilver coal absorbent charcoal that makes.
As shown in Figure 1, 2, described absorbent charcoal cleaning machine comprises that frame 1, discharge outlet 2, net cage 3, conveying device 4, bubble type cleaning add sluicing device 5, deviation correcting device 6, spray rinsing device 7, wind and bounce doffer 8, microseism water logging device 9 and hopper 10.Frame 1 both sides are provided with discharge outlet 2, conveying device 4 is arranged on the frame 1, above conveying device 4, be disposed with net cage 3, deviation correcting device 6, spray rinsing device 7, wind from left to right and bounce doffer 8, net cage 3 places are provided with the bubble type cleaning and add sluicing device 5, wind is provided with hopper 10 with the below of bouncing doffer 8, and hopper 10 belows are provided with microseism water logging device 9.
Net cage 3 is located at the horizontal segment top on conveying device 4 left sides, and net cage 3 is 20 purpose stainless steel guipures.Active carbon to be cleaned is placed on the net cage 3, above net cage 3, be provided with two sparge pipes that are parallel to net cage 3 planes, be connected with water tank on the sparge pipe water inlet end, the water tank water intake end is connected with water pump, sparge pipe is provided with nozzle, nozzle washes away active carbon towards the traffic direction of conveying device 4 so that the current of nozzle clean, and simultaneously active carbon is promoted forward.In the both sides of net cage 3 tracheae is installed respectively, be connected with air pump on the tracheae, every tracheae is provided with plurality of nozzles, the tracheae nozzle tilts towards the traffic direction of conveying device 4, the tracheae nozzle becomes 45 degree directions approximately with tracheae, the bubble of tracheae nozzle ejection fully makes activated carbon granule seethe, the current that sprayed by the sparge pipe nozzle clean and wash away simultaneously, the bubble of tracheae and the current of sparge pipe together promote activated carbon granule and arrive next device forward, be on the intermediate, inclined section of conveying device 4, the step of going forward side by side cleans.
Net cage 3 overlaps by silicane rubber plate with conveying device 4 intermediate, inclined sections, be provided with deviation correcting device 6 in the zone of the two connection, described deviation correcting device 6 is for respectively being provided with a water pipe in the both sides of join domain, every water pipe is provided with 3～4 water spouts, described water pipe cleans the water tank that adds sluicing device 5 with bubble type and links to each other, before water spout is tilted to, towards the traffic direction of conveying device 4, current with the water spout ejection are corrected the active carbon of going on the selvage, make it not run material.
Above conveying device 4 intermediate, inclined sections, be provided with spray rinsing device 7, described spray rinsing device 7 comprises five spray headers, each spray header is provided with four spray nozzles, spray nozzle faces the active carbon on the conveyer belt, spray header is connected with the reverse osmose pure-water water pump, the water of being imported is for directly reaching the reverse osmose pure-water of drinking water standard, reverse osmosis water (water will reach the direct drinking water requirement) electrical conductivity is controlled at below the 12us/cm, spray rinsing device 7 further cleaning active charcoals, and can clean supplementing water in the water tank add sluicing device 5 to bubble type, be used for doing first step bubble type and clean the cleaning flush water that adds in the sluicing and recycle.
Horizontal segment place, conveying device 4 the right is provided with wind and bounces doffer 8, wind with bounce doffer 8 and comprise that the blower fan that is separately positioned on conveying device 4 the right horizontal segments top and three off-centre of below bounce device, described off-centre is bounced device for three groups of eccentric hammer are installed on turning cylinder, one group of symmetrical mounting of per two eccentric hammer is on turning cylinder, and turning cylinder is by motor drives.
On wind and the frame 1 of bouncing relevant position below the doffer 8, be provided with hopper 10, in order to the activated carbon granule of carrying from conveying device 4 through cleaning.On the ground of hopper 10 below correspondence positions microseism water logging device 9 is arranged, bounce the guipure that device bounces conveying device 4 with off-centre, the active carbon that is bonded on the guipure is separated and be sent on the hopper 10, and slide in the microseism water logging device 9 that is arranged on hopper 10 belows through hopper 10.Microseism water logging device 9 comprises Turnround basket, is provided with an eccentric bobbing machine on Turnround basket, and Turnround basket is the frame of plastic of 200Kg level 20 order meshes, washes away the portion of water of adsorbing in the process by bobbing machine vibration drop deactivation charcoal in cleaning.Conveying device 4 comprises carrying band, transmission guipure, wallboard, silicane rubber plate, motor, the carrying band is superimposed upon on the transmission guipure, carrying band both sides are provided with wallboard, between carrying band and wallboard, be provided with silicane rubber plate, prevent that active carbon from running material in transmission process, conveying device 4 is by motor drives, and described carrying band is a stainless steel herringbone band, and the transmission guipure is 20 order stainless steel guipures.Motor drives off-centre is bounced the turning cylinder of device, the power transmission shaft motion of conveying device 4.
Shown in Fig. 3,4, described drying machine is a band drier, comprises transmission guipure 31, main tank 32, side case 33, blower fan 34, hopper 35, dry dehumidification tube 36.In the drying machine casing, be provided with transmission guipure 31, the working width of transmission guipure 31 is 0.6 meter, active length is 8 meters, transmission guipure 31 also plays simultaneously the carrying effect so adopt bilayer to be laminated with guipure playing transmission, promptly carrying guipure is superimposed upon on the foraminous conveyer, bearer network adopts stainless steel herringbone band, and foraminous conveyer adopts 20 order stainless steel guipures.In transmission process, run material for preventing active carbon, be provided with y-shaped ring in transmission guipure 31 both sides, with y-shaped ring come restricted activity charcoal particle in transmission process owing to material is run in wind, activated carbon granule is gathered to the centre.Cabinet both sides at drying machine are provided with access door, convenient maintenance, maintenance, and dry tenacity is 5.2Kg
Water/ m
2H.The complete equipment of drying machine is divided into main tank 32 and side case 33, simultaneously material is carried out drying by two drying systems in master, the side case, main, side case is separated into five unit, be provided with blower fan 34 in each unit, blower fan 34 cooperates with electrical heating, infrared ray heating system, material is blown out hot blast carry out drying.Main tank 32, side case are provided with split-wind plate in 33 each unit, the hot blast in the main tank 32 is guided for blow to material from the top, hot blast in the side case 33 blows to material from the below, like this when transmission guipure 31 drive materials move in drying machine, upper and lower the passing in turn of hot blast transmitted guipure 31, makes the material that is placed on it be subjected to abundant drying up and down; Electrical heating, the power that infrared ray heating configuration is used is about 36KW, and hot air circulate utilization, the convection heat transfer' heat-transfer by convection in the side railway carriage or compartment 33 have been avoided the direct projection of far red light and have been caused the oxidation and the carbonization of active carbon loading silver.Matching used blower fan 34 is the frequency control blower fan, can regulate wind speed, size as required, the height energy savings.Guipure operates in drying time 24-60min (adjustable) scope employing frequency conversion adjustment+cycloid speed reducer and speed is 1～50m/h coupling (adjustable).End at drying machine is provided with hopper 35, and in order to accept the material that is transported on the drying machine, the discharging opening of hopper 35 is connected with transmission guipure 31.The input end that is provided with hopper at drying machine is provided with dry dehumidification tube 36, since bigger in the moisture humidity of first three unit, so being connected first three unit, 36 of dry dehumidification tubes get final product.Because the wind in the main tank 32 blows from the top down, thus in main tank 32, be connected the bottom of transmission guipure 31; Wind in side case 33 is to blow from bottom to top, thus in side case 33, connect the top of transmission guipure 31.End at transmission guipure 31 has clearing apparatus, is stained with in order to cleaning to be bonded on the transmission guipure 31 and not to be transported to the activated carbon granule of next treating apparatus.
Embodiment 2: get 11 order coal mass active carbon 50kg and clean in absorbent charcoal cleaning machine, then at the drying machine inner drying; With 0.8 gram Ag
4O
4With 1600 gram pH values is that 7.4 sodium hydroxide solution is diluted to solution, is ejected into by constant displacement pump and atomization jetting device on the coal mass active carbon with 80 ℃; With above-mentioned year silver-colored coal mass active carbon in the sealing of 90 ℃ of temperature drying machine against sunshine, carry out drying by the hot blast conduction, last under 15 minutes time conditions, make the 50Kg tetroxide tetrsilver coal absorbent charcoal, contain the 0.7g Tetrasilver tetroxide in the 50Kg tetroxide tetrsilver coal absorbent charcoal that makes.
Embodiment 3: get 9 order coal mass active carbon 80kg and clean in absorbent charcoal cleaning machine, then at the drying machine inner drying; 1 gram Ag
4O
4With 1250 gram pH values is that 7.5 aqua calcis solvent dilution becomes solution, sprays on the 80Kg coal mass active carbon with 75 ℃ of cleanings; In the sealing of 85 ℃ of temperature drying machine against sunshine, by blower fan, far infrared heating drying, the frequency control blower fan: the 11Hz drying, last 14 fens clock times, make the 80Kg tetroxide tetrsilver coal absorbent charcoal, contain the 0.9g Tetrasilver tetroxide in the 80Kg tetroxide tetrsilver coal absorbent charcoal that makes.
The absorbent charcoal cleaning machine of embodiment 2,3, drying machine are with embodiment 1.
Tetroxide tetrsilver coal absorbent charcoal has wide application prospect in drinking water treatment, utilize the water treatment facilities of tetroxide tetrsilver coal absorbent charcoal production to have following characteristics: (1) former water use efficiency height (99%), no waste water is discharged.(2) occupation area of equipment is little, power consumption is little, meet water saving, saves land energy-conservation principle.(3) natural, the mineral of water quality, activity, long-acting bacteriostatic meet the standard of healthy drinking water.(4) equipment can self-pollution; need not equipment and the water disinfection after handling; in the production technology of bucket bottled water, removed ozone devices; satisfied cleaner production; the protection environment requirement is worked the production operation personnel, and is adopted the water treatment system of tetroxide tetrsilver coal absorbent charcoal of the present invention under the environment of a safety; operating cost is low, and investment repayment is fast.
Adopt tetroxide tetrsilver coal absorbent charcoal of the present invention in water purifier and direct drinking water supply project equipment as other material in the application of filtering material and the existing water treatment facilities as the contrast of the effect of filtering material:
Contrast " drinking water standard " (GB5749-2006), according to " the drinking water standard method of inspection " (GB5750-2006) to the former water of above-mentioned customization, use wood activated charcoal respectively, coal mass active carbon, the Tetrasilver tetroxide cocoanut active charcoal, tetroxide tetrsilver coal absorbent charcoal is placed on as filtering material and does dynamically " pillar " experiment in the water purifier, measured targetedly to begin a project, find tetroxide tetrsilver coal absorbent charcoal absorption look, processing turbidity etc. all is better than other several active carbons, and coal mass active carbon draw materials wide and price far below cocoanut active charcoal, so reduced cost, be easy to vigorously promote the use.
Claims (7)
1, a kind of tetroxide tetrsilver coal absorbent charcoal is characterized in that: it comprises coal mass active carbon and Tetrasilver tetroxide, and described Tetrasilver tetroxide adsorbed close is in the aperture of the surface of coal mass active carbon or active carbon.
2, tetroxide tetrsilver coal absorbent charcoal according to claim 1 is characterized in that: the Tetrasilver tetroxide content in per 100 gram tetroxide tetrsilver coal absorbent charcoals is not less than 0.1 milligram.
3, tetroxide tetrsilver coal absorbent charcoal according to claim 1 and 2 is characterized in that: described coal mass active carbon is 9～11 orders.
4, the preparation method of the described tetroxide tetrsilver coal absorbent charcoal of claim 1 is characterized in that: comprise the steps:
1) coal mass active carbon cleaning and dry back is standby; Is that 0.5～1 ‰ ratio is mixed with Tetrasilver tetroxide and pH value by weight at 7.0～7.5 alkalescent solvent;
2) mixed liquor in the step 1) is sprayed to temperature on 50～80 ℃ coal mass active carbon;
3) with step 2) in make carry silver-colored coal mass active carbon under 70～90 ℃, sealing equipment inner drying against sunshine 8～15 minutes, promptly obtain tetroxide tetrsilver coal absorbent charcoal.
5, the preparation method of tetroxide tetrsilver coal absorbent charcoal according to claim 4 is characterized in that: the alkalescent solvent described in the step 1) is a kind of in ammoniacal liquor, sodium hydroxide solution, the aqua calcis.
6, the preparation method of tetroxide tetrsilver coal absorbent charcoal according to claim 4 is characterized in that: described coal mass active carbon is 9～11 orders.
7, tetroxide tetrsilver coal absorbent charcoal is as the application of filtering material in water purifier and direct drinking water supply project equipment.
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNA2008100219066A CN101342480A (en) | 2008-08-18 | 2008-08-18 | Tetroxide tetrsilver coal absorbent charcoal, preparation method and uses thereof |
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|---|---|---|---|
| CNA2008100219066A CN101342480A (en) | 2008-08-18 | 2008-08-18 | Tetroxide tetrsilver coal absorbent charcoal, preparation method and uses thereof |
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Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102114408A (en) * | 2011-01-06 | 2011-07-06 | 苏州邦安新材料科技有限公司 | Silver-loaded active carbon and rheological phase preparation process thereof |
| CN102173477A (en) * | 2011-01-06 | 2011-09-07 | 苏州邦安新材料科技有限公司 | Preparation technique of novel silver-carried activated carbon by hydrothermal method |
| CN101767905B (en) * | 2009-12-30 | 2012-12-05 | 扬州大学 | City landscape water body alga-controlling and pollutant-removing device |
| CN111054309A (en) * | 2019-12-30 | 2020-04-24 | 南通得力净化器材厂有限公司 | Formaldehyde-removing carbon cotton modification production device and use method thereof |
-
2008
- 2008-08-18 CN CNA2008100219066A patent/CN101342480A/en active Pending
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101767905B (en) * | 2009-12-30 | 2012-12-05 | 扬州大学 | City landscape water body alga-controlling and pollutant-removing device |
| CN102114408A (en) * | 2011-01-06 | 2011-07-06 | 苏州邦安新材料科技有限公司 | Silver-loaded active carbon and rheological phase preparation process thereof |
| CN102173477A (en) * | 2011-01-06 | 2011-09-07 | 苏州邦安新材料科技有限公司 | Preparation technique of novel silver-carried activated carbon by hydrothermal method |
| CN102114408B (en) * | 2011-01-06 | 2013-04-03 | 苏州邦安新材料科技有限公司 | Silver-loaded active carbon and rheological phase preparation process thereof |
| CN102173477B (en) * | 2011-01-06 | 2014-02-19 | 苏州泰利三佳纳米科技有限公司 | Preparation technique of novel silver-carried activated carbon by hydrothermal method |
| CN111054309A (en) * | 2019-12-30 | 2020-04-24 | 南通得力净化器材厂有限公司 | Formaldehyde-removing carbon cotton modification production device and use method thereof |
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Open date: 20090114 |