CN107265527A - Composite water purifying agent and its application are prepared using aluminium scrap lime-ash - Google Patents
Composite water purifying agent and its application are prepared using aluminium scrap lime-ash Download PDFInfo
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- CN107265527A CN107265527A CN201710612325.9A CN201710612325A CN107265527A CN 107265527 A CN107265527 A CN 107265527A CN 201710612325 A CN201710612325 A CN 201710612325A CN 107265527 A CN107265527 A CN 107265527A
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
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- Environmental & Geological Engineering (AREA)
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Abstract
Composite water purifying agent and its application are prepared using aluminium scrap lime-ash the invention discloses one kind, belongs to water purification agent preparing technical field.The present invention is using aluminium scrap lime-ash as raw material, filter and air-dry after being mixed with distilled water, add limestone powder calcining and be ground into particle, mixed with sulfuric acid, manganese dioxide heating, standing filters to get filtrate, add ferric sulfate and glycerine heating stirring, sodium oxide molybdena hydrolytic polymerization is added, curing is stood, mixed with distilled water until being produced without precipitation, filtrate is filtered to obtain, drying, which is crushed, is made composite water purifying agent.The beneficial effects of the invention are as follows：The present invention makes full use of aluminium scrap lime-ash to prepare water purification agent, not only solves problem of environmental pollution, also achieves the sustainable use of resource；Gained water purification agent is produced in Water treatment without any new solid waste, and post-processing is simple, cost is low, and water purification rate is higher than other water purification agents more than 32%.
Description
Technical field
The present invention relates to a kind of method that utilization aluminium scrap lime-ash prepares composite water purifying agent, belong to water purification agent technology of preparing neck
Domain.
Background technology
Aluminium ash is mainly generated during aluminum oxide produces aluminium through molten-salt electrolysis, due to operating and measuring instrument is taken
Band, anode change, go out the reasons such as aluminium, ingot casting and electrolytic cell overhaul, substantial amounts of aluminium slag can be produced.Typically often producing 1 ton of aluminium will
Produce 3050 kilograms of aluminium slag aluminium ashes.In recent years, China's aluminium production capacity and yield are increased considerably.Again, aluminium scrap regeneration is laid equal stress on
The rate of recovery of new fabricated product is generally 75%~85%.1 ton of aluminium scrap of regeneration will produce 150~250 kilograms of aluminium slag aluminium ashes.Aluminium lime-ash
It is a kind of renewable resource, but does not obtain one of enough attention, the factor as welding always.With economic hair
Exhibition, aluminium scrap lime-ash accumulation is increased considerably year by year, if the method for not finding economical and effective and environmental protection is administered, its is right
The serious threat of environment will be highlighted increasingly.The grey Slag treatment rate of recovery of China's aluminum current is low, and energy expenditure is big, and research and development will
Industrial aluminum lime-ash reclaim prepares other materials, for increasing economic efficiency, preserve the ecological environment have important practical significance with
Practical value.
Water purification agent is exactly to deliver energy and other aitiogenic medicaments of impurity in water in water.Mainly play the mesh of water purification
's.Water purification agent is generally produced using flyash at present, but this method is high due to flyash production temperature, aluminium element therein is very
Hardly possible is leached with strong acid, and cosolvent fluoride need to be added to improve the extraction rate of aluminium, and processing cost is improved due to introducing fluoride,
And new solid waste can be produced during production water purification agent, the solid waste is the raw material for producing sodium metasilicate again, or production is in vain
The raw material of carbon black and zeolite, equipment and raw material that its post-order process need to be new, post-processing is complex and high cost.Therefore one is worked out
The method that water purification agent is prepared using aluminium scrap lime-ash is planted, with important practical value.
The content of the invention
The technical problems to be solved by the invention：Low for the grey Slag treatment rate of recovery of aluminum current, energy expenditure is big, pollutes ring
Border, and current water purification agent can produce new solid waste in Water treatment, the drawbacks of post-processing is complicated, cost is high is carried
One kind has been supplied using aluminium scrap lime-ash as raw material, has filtered and air-dries after being mixed with distilled water, limestone powder calcining has been added and is ground into particle,
Mixed with sulfuric acid, manganese dioxide heating, standing filters to get filtrate, and adds ferric sulfate and glycerine heating stirring, adds sodium oxide molybdena
Hydrolytic polymerization, stands curing, mixes and is produced up to without precipitation with distilled water, filters to obtain filtrate, and drying, which is crushed, to be made
The method of composite water purifying agent.The present invention is high to the grey Slag treatment rate of recovery of aluminium, and products obtained therefrom is consolidated in Water treatment without any new
Body waste is produced, and purifying water effect is good.
In order to solve the above technical problems, the present invention is using technical scheme as described below：
（1）Take 1~3kg aluminium scrap lime-ash to be put into container, distillation water submerged aluminium scrap 2~3cm of lime-ash is added thereto, with rotating speed
Filtered after 200~300r/min, 20~30min of stirring, then the aluminium scrap lime-ash after filtering be put into air-dry machine and air-dried,
Subsequent in mass ratio 2:1, it is well mixed with 60 mesh limestone powders；
（2）Above-mentioned mixture is put into calcining furnace and calcined, temperature control is 700~800 DEG C, calcines 1~2h, then
Temperature in use carries out being cooled to room temperature for 0~5 DEG C of hydrogen to it, then puts the aluminium scrap lime-ash of the pretreatment obtained after cooling
Enter in pulverizer and crushed, cross standard screen and obtain 80~100 mesh particulate matters；
（3）The particulate matter of above-mentioned gained is put into container, mass fraction is added thereto and is flooded for 65~70% sulfuric acid solution
Do not have 2~4cm of particulate matter, while adding the hydrogen peroxide that mass fraction is 30%, addition is the 20~30% of sulfuric acid solution volume,
After stirring, then manganese dioxide is added thereto, addition is the 2~4% of aluminium scrap lime-ash quality, and then container is added
Heat, it is 70~80 DEG C to be heated to temperature, and speed setting is 160~210r/min；
（4）After after above-mentioned 2~5h of stirring, 40~50 DEG C are cooled to, is discharged the air in container using nitrogen, sealing container,
Stand and filtered after 30~40min, collect filtered fluid, the filtered fluid of gained is put into three-necked flask, then is added thereto respectively
Mass fraction is 55% ferrum sulfuricum oxydatum solutum, and addition is the 70~80% of filtered fluid volume, and 600~900mL glycerine, then
Three-necked flask is heated, temperature is heated to for 110~120 DEG C, while being stirred with 150~180r/min rotating speed；
（5）After after above-mentioned 2~4h of heating stirring, adding 100~200g sodium oxide molybdenas thereto, addition speed is 3~5g/min, oxygen
Change sodium addition to finish, stop heating after 1~2h of hydrolytic polymerization, stand 20~26h of curing, obtain pale red brown liquid, add thereto
Enter the distilled water that temperature is 5~10 DEG C, stirring is produced up to deposit-free, then filtered, and filtrate is collected, by filtrate
It is put into baking oven and dries, place into pulverizer and crushed, cross standard screen and obtain 40~80 mesh particles, you can obtains compound water purification
Agent.
The application process of the present invention：300~500NTUI of composite water purifying agent input raw water turbidity obtained by the present invention is dirty
In water, input amount is 3~5mg/L, 20~30min is stirred in the case where rotating speed is 200~400r/min, then reduce rotating speed for 80r/
Min stirs 10~20min, stands 1~2h, detection water outlet SS≤16mg/L, delivery turbidity is 20~25NTUI, in Water treatment
It is middle to be produced without any new solid waste.
The present invention is compared with other method, and advantageous effects are：
（1）The present invention makes full use of aluminium scrap lime-ash to prepare water purification agent, not only solves problem of environmental pollution, also achieves resource
Sustainable use；
（2）Gained water purification agent is produced in Water treatment without any new solid waste, and post-processing is simple, cost is low, water purification
Rate is higher than other water purification agents more than 32%.
Embodiment
Take 1~3kg aluminium scrap lime-ash to be put into container first, distillation water submerged aluminium scrap 2~3cm of lime-ash added thereto,
With 200~300r/min of rotating speed, filtered after 20~30min of stirring, then be put into air-dry machine by the aluminium scrap lime-ash after filtering
Sector-style is done, and then in mass ratio 2:1, it is well mixed with 60 mesh limestone powders；Then above-mentioned mixture is put into calcining furnace
Middle to be calcined, temperature control is 700~800 DEG C, calcines 1~2h, and then temperature in use is carried out for 0~5 DEG C of hydrogen to it
Room temperature is cooled to, then the aluminium scrap lime-ash of the pretreatment obtained after cooling is put into pulverizer and crushed, standard screen is crossed and obtains
80~100 mesh particulate matters；The particulate matter of above-mentioned gained is put into container again, it is 65~70% that mass fraction is added thereto
Sulfuric acid solution floods 2~4cm of particulate matter, while adding the hydrogen peroxide that mass fraction is 30%, addition is sulfuric acid solution volume
20~30%, after stirring, then add manganese dioxide thereto, addition is the 2~4% of aluminium scrap lime-ash quality, then
Container is heated, it is 70~80 DEG C to be heated to temperature, speed setting is 160~210r/min；Treat above-mentioned 2~5h of stirring
Afterwards, 40~50 DEG C are cooled to, is discharged the air in container using nitrogen, sealing container, stands and is filtered after 30~40min, received
Collect filtered fluid, the filtered fluid of gained is put into three-necked flask, then add the ferric sulfate that mass fraction is 55% thereto respectively
Solution, addition is the 70~80% of filtered fluid volume, and 600~900mL glycerine, and then three-necked flask is heated, plus
Heat to temperature is 110~120 DEG C, while being stirred with 150~180r/min rotating speed；Finally treat above-mentioned heating stirring 2~
After 4h, 100~200g sodium oxide molybdenas are added thereto, and addition speed is 3~5g/min, and sodium oxide molybdena is added and finished, hydrolytic polymerization 1~
Stop heating after 2h, stand 20~26h of curing, obtain pale red brown liquid, the distilled water that temperature is 5~10 DEG C is added thereto,
Stirring is until deposit-free generation, is then filtered, and filtrate is put into baking oven and dried, places into powder by collection filtrate
Crushed in broken machine, cross standard screen and obtain 40~80 mesh particles, you can obtain composite water purifying agent.
Example 1
Take 1kg aluminium scrap lime-ash to be put into container first, distillation water submerged aluminium scrap lime-ash 2cm is added thereto, with rotating speed 200r/
Filtered after min, stirring 20min, then the aluminium scrap lime-ash after filtering is put into air-dry machine and air-dried, then in mass ratio 2:
1, it is well mixed with 60 mesh limestone powders；Then above-mentioned mixture is put into calcining furnace and calcined, temperature control is
700 DEG C, 1h is calcined, then temperature in use carries out being cooled to room temperature for 0 DEG C of hydrogen to it, then by the pre- place obtained after cooling
The aluminium scrap lime-ash of reason, which is put into pulverizer, to be crushed, and is crossed standard screen and is obtained 80 mesh particulate matters；The particulate matter of above-mentioned gained is put again
Enter in container, mass fraction is added thereto and floods particulate matter 2cm for 65% sulfuric acid solution, while addition mass fraction is
30% hydrogen peroxide, addition is the 20% of sulfuric acid solution volume, after stirring, then adds manganese dioxide thereto, is added
Measure as the 2% of aluminium scrap lime-ash quality, then container is heated, be heated to temperature for 70 DEG C, speed setting is 160r/min；
After after above-mentioned stirring 2h, 40 DEG C are cooled to, is discharged the air in container using nitrogen, sealing container, mistake after 30min is stood
Filter, collects filtered fluid, the filtered fluid of gained is put into three-necked flask, then adds the sulphur that mass fraction is 55% thereto respectively
Sour ferrous solution, addition is the 70% of filtered fluid volume, and 600mL glycerine, and then three-necked flask is heated, temperature is heated to
Spend for 110 DEG C, while being stirred with 150r/min rotating speed；Finally after after above-mentioned heating stirring 2h, 100g is added thereto
Sodium oxide molybdena, addition speed is 3g/min, and sodium oxide molybdena is added and finished, and stops heating after hydrolytic polymerization 1h, stands curing 20h, obtains shallow
Rufous liquid, adds the distilled water that temperature is 5 DEG C thereto, and stirring is produced up to deposit-free, then filtered, and is collected
Filtrate, filtrate is put into baking oven and dried, places into pulverizer and is crushed, and is crossed standard screen and is obtained 40 mesh particles, you can
Obtain composite water purifying agent.
By in the composite water purifying agent input raw water turbidity 300NTUI sewage obtained by the present invention, input amount is 3mg/L,
Rotating speed is to stir 20min under 200r/min, then reduces rotating speed and stir 10min for 80r/min, stands 1h, detection water outlet SS is
16mg/L, delivery turbidity is 20NTUI, is produced in Water treatment without any new solid waste.
Example 2
Take 2kg aluminium scrap lime-ash to be put into container first, distillation water submerged aluminium scrap lime-ash 2.5cm is added thereto, with rotating speed
Filtered after 250r/min, stirring 25min, then the aluminium scrap lime-ash after filtering is put into air-dry machine and air-dried, then by matter
Amount compares 2:1, it is well mixed with 60 mesh limestone powders；Then above-mentioned mixture is put into calcining furnace and calcined, temperature
Control as 750 DEG C, calcine 1.5h, then temperature in use carries out being cooled to room temperature for 3 DEG C of hydrogen to it, after then cooling down
To the aluminium scrap lime-ash of pretreatment be put into pulverizer and crushed, cross standard screen and obtain 90 mesh particulate matters；Again by above-mentioned gained
Particulate matter is put into container, and mass fraction is added thereto and floods particulate matter 3cm for 68% sulfuric acid solution, while adding quality
Fraction is 30% hydrogen peroxide, and addition is the 25% of sulfuric acid solution volume, after stirring, then adds titanium dioxide thereto
Manganese, addition is the 3% of aluminium scrap lime-ash quality, and then container is heated, and it is 75 DEG C to be heated to temperature, and speed setting is
185r/min；After after above-mentioned stirring 3.5h, 45 DEG C are cooled to, is discharged the air in container using nitrogen, sealing container, is stood
Filtered after 35min, collect filtered fluid, the filtered fluid of gained is put into three-necked flask, then add mass fraction thereto respectively
For 55% ferrum sulfuricum oxydatum solutum, addition is the 75% of filtered fluid volume, and 750mL glycerine, and then three-necked flask is added
Heat, is heated to temperature for 115 DEG C, while being stirred with 165r/min rotating speed；Finally after after above-mentioned heating stirring 3h, Xiang Qi
Middle addition 150g sodium oxide molybdenas, addition speed is 4g/min, and sodium oxide molybdena is added and finished, and stops heating after hydrolytic polymerization 1.5h, is stood
23h is cured, pale red brown liquid is obtained, the distilled water that temperature is 8 DEG C, stirring are added thereto until deposit-free is produced, then
Filtered, collect filtrate, filtrate is put into baking oven and dried, places into pulverizer and is crushed, crossed standard screen and obtain
60 mesh particles, you can obtain composite water purifying agent.
By in the composite water purifying agent input raw water turbidity 400NTUI sewage obtained by the present invention, input amount is 4mg/L,
Rotating speed is to stir 25min under 300r/min, then reduces rotating speed and stir 15min for 80r/min, stands 1.5h, detection water outlet SS is
15.1mg/L, delivery turbidity is 22NTUI, is produced in Water treatment without any new solid waste.
Example 3
Take 3kg aluminium scrap lime-ash to be put into container first, distillation water submerged aluminium scrap lime-ash 3cm is added thereto, with rotating speed 300r/
Filtered after min, stirring 30min, then the aluminium scrap lime-ash after filtering is put into air-dry machine and air-dried, then in mass ratio 2:
1, it is well mixed with 60 mesh limestone powders；Then above-mentioned mixture is put into calcining furnace and calcined, temperature control is
800 DEG C, 2h is calcined, then temperature in use carries out being cooled to room temperature for 5 DEG C of hydrogen to it, then by the pre- place obtained after cooling
The aluminium scrap lime-ash of reason, which is put into pulverizer, to be crushed, and is crossed standard screen and is obtained 100 mesh particulate matters；The particulate matter of above-mentioned gained is put again
Enter in container, mass fraction is added thereto and floods particulate matter 4cm for 70% sulfuric acid solution, while addition mass fraction is
30% hydrogen peroxide, addition is the 30% of sulfuric acid solution volume, after stirring, then adds manganese dioxide thereto, is added
Measure as the 4% of aluminium scrap lime-ash quality, then container is heated, be heated to temperature for 80 DEG C, speed setting is 210r/min；
After after above-mentioned stirring 5h, 50 DEG C are cooled to, is discharged the air in container using nitrogen, sealing container, mistake after 40min is stood
Filter, collects filtered fluid, the filtered fluid of gained is put into three-necked flask, then adds the sulphur that mass fraction is 55% thereto respectively
Sour ferrous solution, addition is the 80% of filtered fluid volume, and 900mL glycerine, and then three-necked flask is heated, temperature is heated to
Spend for 120 DEG C, while being stirred with 180r/min rotating speed；Finally after after above-mentioned heating stirring 4h, 200g is added thereto
Sodium oxide molybdena, addition speed is 5g/min, and sodium oxide molybdena is added and finished, and stops heating after hydrolytic polymerization 2h, stands curing 26h, obtains shallow
Rufous liquid, adds the distilled water that temperature is 10 DEG C thereto, and stirring is produced up to deposit-free, then filtered, and is received
Collect filtrate, filtrate is put into baking oven and dried, places into pulverizer and is crushed, cross standard screen and obtain 80 mesh particles, i.e.,
It can obtain composite water purifying agent.
By in the composite water purifying agent input raw water turbidity 500NTUI sewage obtained by the present invention, input amount is 5mg/L,
Rotating speed is to stir 30min under 400r/min, then reduces rotating speed and stir 20min for 80r/min, stands 2h, detection water outlet SS is
14.2mg/L, delivery turbidity is 25NTUI, is produced in Water treatment without any new solid waste.
Claims (1)
1. a kind of utilization aluminium scrap lime-ash prepares the application process of composite water purifying agent, it is characterised in that the water purification agent is by specific as follows
Preparation process is made：
（1）Take 1~3kg aluminium scrap lime-ash to be put into container, distillation water submerged aluminium scrap 2~3cm of lime-ash is added thereto, with rotating speed
Filtered after 200~300r/min, 20~30min of stirring, then the aluminium scrap lime-ash after filtering be put into air-dry machine and air-dried,
Subsequent in mass ratio 2:1, it is well mixed with 60 mesh limestone powders；
（2）Above-mentioned mixture is put into calcining furnace and calcined, temperature control is 700~800 DEG C, calcines 1~2h, then
Temperature in use carries out being cooled to room temperature for 0~5 DEG C of hydrogen to it, then puts the aluminium scrap lime-ash of the pretreatment obtained after cooling
Enter in pulverizer and crushed, cross standard screen and obtain 80~100 mesh particulate matters；
（3）The particulate matter of above-mentioned gained is put into container, mass fraction is added thereto and is flooded for 65~70% sulfuric acid solution
Do not have 2~4cm of particulate matter, while adding the hydrogen peroxide that mass fraction is 30%, addition is the 20~30% of sulfuric acid solution volume,
After stirring, then manganese dioxide is added thereto, addition is the 2~4% of aluminium scrap lime-ash quality, and then container is added
Heat, it is 70~80 DEG C to be heated to temperature, and speed setting is 160~210r/min；
（4）After after above-mentioned 2~5h of stirring, 40~50 DEG C are cooled to, is discharged the air in container using nitrogen, sealing container,
Stand and filtered after 30~40min, collect filtered fluid, the filtered fluid of gained is put into three-necked flask, then is added thereto respectively
Mass fraction is 55% ferrum sulfuricum oxydatum solutum, and addition is the 70~80% of filtered fluid volume, and 600~900mL glycerine, then
Three-necked flask is heated, temperature is heated to for 110~120 DEG C, while being stirred with 150~180r/min rotating speed；
（5）After after above-mentioned 2~4h of heating stirring, adding 100~200g sodium oxide molybdenas thereto, addition speed is 3~5g/min, oxygen
Change sodium addition to finish, stop heating after 1~2h of hydrolytic polymerization, stand 20~26h of curing, obtain pale red brown liquid, add thereto
Enter the distilled water that temperature is 5~10 DEG C, stirring is produced up to deposit-free, then filtered, and filtrate is collected, by filtrate
It is put into baking oven and dries, place into pulverizer and crushed, cross standard screen and obtain 40~80 mesh particles, you can obtains compound water purification
Agent；
Described application process：Composite water purifying agent obtained by the present invention is put into raw water turbidity 300~500NTUI sewage,
Input amount is 3~5mg/L, and 20~30min is stirred in the case where rotating speed is 200~400r/min, then reduces rotating speed and is stirred for 80r/min
10~20min, stands 1~2h, detection water outlet SS≤16mg/L, delivery turbidity is 20~25NTUI, and nothing is appointed in Water treatment
He Xin solid waste is produced.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710612325.9A CN107265527A (en) | 2015-12-01 | 2015-12-01 | Composite water purifying agent and its application are prepared using aluminium scrap lime-ash |
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710612325.9A CN107265527A (en) | 2015-12-01 | 2015-12-01 | Composite water purifying agent and its application are prepared using aluminium scrap lime-ash |
| CN201510865151.8A CN105314693B (en) | 2015-12-01 | 2015-12-01 | A kind of method that utilization aluminium scrap lime-ash prepares composite water purifying agent |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201510865151.8A Division CN105314693B (en) | 2015-12-01 | 2015-12-01 | A kind of method that utilization aluminium scrap lime-ash prepares composite water purifying agent |
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| CN107265527A true CN107265527A (en) | 2017-10-20 |
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| CN201510865151.8A Expired - Fee Related CN105314693B (en) | 2015-12-01 | 2015-12-01 | A kind of method that utilization aluminium scrap lime-ash prepares composite water purifying agent |
| CN201710613914.9A Pending CN107188255A (en) | 2015-12-01 | 2015-12-01 | One kind prepares composite water purifying agent using aluminium scrap lime-ash |
| CN201710612325.9A Pending CN107265527A (en) | 2015-12-01 | 2015-12-01 | Composite water purifying agent and its application are prepared using aluminium scrap lime-ash |
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| CN201510865151.8A Expired - Fee Related CN105314693B (en) | 2015-12-01 | 2015-12-01 | A kind of method that utilization aluminium scrap lime-ash prepares composite water purifying agent |
| CN201710613914.9A Pending CN107188255A (en) | 2015-12-01 | 2015-12-01 | One kind prepares composite water purifying agent using aluminium scrap lime-ash |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108408923A (en) * | 2018-04-17 | 2018-08-17 | 合肥金同维低温科技有限公司 | A kind of purifying agent and preparation method thereof |
Families Citing this family (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106396051A (en) * | 2016-06-23 | 2017-02-15 | 江门市江海区炜洁净水材料有限公司 | A method of preparing a composite water purifier by utilizing scrap iron clinker |
| CN106745130A (en) * | 2017-01-11 | 2017-05-31 | 西北农林科技大学 | A kind of method that aluminium lime-ash prepares aluminum oxide |
| CN106745128A (en) * | 2017-01-11 | 2017-05-31 | 西北农林科技大学 | A kind of method of aluminium lime-ash removal of impurities |
| CN107470318B (en) * | 2017-07-07 | 2020-07-28 | 南通大学 | Aluminum ash step utilization device |
| CN107398465A (en) * | 2017-07-27 | 2017-11-28 | 区耀垣 | A kind of processing method of aluminium ash |
| CN111360031A (en) * | 2020-03-19 | 2020-07-03 | 靳六旦 | Waste aluminum ash treatment process |
| CN112121611A (en) * | 2020-09-24 | 2020-12-25 | 西南科技大学 | Method for preparing cement kiln flue gas purifying agent from aluminum ash |
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|---|---|---|---|---|
| JPS6339309B2 (en) * | 1980-07-04 | 1988-08-04 | Ebara Infilco | |
| CN101913634A (en) * | 2010-08-28 | 2010-12-15 | 河南科泰净水材料有限公司 | Processing method for recycling aluminum dross |
| CN103523834A (en) * | 2013-10-18 | 2014-01-22 | 乔占印 | Process for preparing rare earth polymeric aluminum ferric sulfate by using rare earth tailing waste slag |
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| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| KR20010088729A (en) * | 2001-03-15 | 2001-09-28 | 제창국 | A solid clarifier manufactured by a natural inorganic element |
| CN102815778B (en) * | 2012-08-31 | 2014-06-04 | 广州博芳环保科技有限公司 | Preparation method of environment-friendly phosphorous removing agent |
| CN104692503A (en) * | 2013-12-04 | 2015-06-10 | 青岛浩泰水务有限公司 | Environmentally-friendly aluminum salt-containing water purification agent |
| CN104310547A (en) * | 2014-10-17 | 2015-01-28 | 陕西华陆化工环保有限公司 | Method for preparing flocculating agent by utilizing aluminium smelting ash as raw material |
-
2015
- 2015-12-01 CN CN201510865151.8A patent/CN105314693B/en not_active Expired - Fee Related
- 2015-12-01 CN CN201710613914.9A patent/CN107188255A/en active Pending
- 2015-12-01 CN CN201710612325.9A patent/CN107265527A/en active Pending
Patent Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS6339309B2 (en) * | 1980-07-04 | 1988-08-04 | Ebara Infilco | |
| CN101913634A (en) * | 2010-08-28 | 2010-12-15 | 河南科泰净水材料有限公司 | Processing method for recycling aluminum dross |
| CN103523834A (en) * | 2013-10-18 | 2014-01-22 | 乔占印 | Process for preparing rare earth polymeric aluminum ferric sulfate by using rare earth tailing waste slag |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108408923A (en) * | 2018-04-17 | 2018-08-17 | 合肥金同维低温科技有限公司 | A kind of purifying agent and preparation method thereof |
Also Published As
| Publication number | Publication date |
|---|---|
| CN105314693B (en) | 2017-10-24 |
| CN105314693A (en) | 2016-02-10 |
| CN107188255A (en) | 2017-09-22 |
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Application publication date: 20171020 |