CN100387532C - Coagulant for disposing dying waste water and its production method - Google Patents
Coagulant for disposing dying waste water and its production method Download PDFInfo
- Publication number
- CN100387532C CN100387532C CNB2005100940554A CN200510094055A CN100387532C CN 100387532 C CN100387532 C CN 100387532C CN B2005100940554 A CNB2005100940554 A CN B2005100940554A CN 200510094055 A CN200510094055 A CN 200510094055A CN 100387532 C CN100387532 C CN 100387532C
- Authority
- CN
- China
- Prior art keywords
- coagulating agent
- weight percentage
- coagulant
- raw material
- acid
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Fee Related
Links
- 239000000701 coagulant Substances 0.000 title claims abstract description 81
- 239000002351 wastewater Substances 0.000 title claims abstract description 30
- 238000004519 manufacturing process Methods 0.000 title abstract description 13
- 239000010881 fly ash Substances 0.000 claims abstract description 28
- 239000002253 acid Substances 0.000 claims abstract description 20
- 238000006243 chemical reaction Methods 0.000 claims abstract description 5
- 238000001816 cooling Methods 0.000 claims abstract description 3
- 229910021645 metal ion Inorganic materials 0.000 claims abstract description 3
- 239000000203 mixture Substances 0.000 claims description 20
- 239000002131 composite material Substances 0.000 claims description 16
- 159000000003 magnesium salts Chemical class 0.000 claims description 13
- RBTARNINKXHZNM-UHFFFAOYSA-K iron trichloride Chemical compound Cl[Fe](Cl)Cl RBTARNINKXHZNM-UHFFFAOYSA-K 0.000 claims description 10
- 239000002994 raw material Substances 0.000 claims description 10
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 claims description 7
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 claims description 6
- 229910052742 iron Inorganic materials 0.000 claims description 5
- 239000012535 impurity Substances 0.000 claims description 4
- 229910052500 inorganic mineral Inorganic materials 0.000 claims description 4
- 239000011707 mineral Substances 0.000 claims description 4
- 239000000126 substance Substances 0.000 claims description 4
- 239000000725 suspension Substances 0.000 claims description 4
- 229910004298 SiO 2 Inorganic materials 0.000 claims description 3
- 150000001875 compounds Chemical class 0.000 claims description 3
- 239000000428 dust Substances 0.000 claims description 3
- 239000007788 liquid Substances 0.000 claims description 3
- 238000002386 leaching Methods 0.000 claims description 2
- 238000004043 dyeing Methods 0.000 abstract description 24
- 238000005516 engineering process Methods 0.000 abstract description 8
- 238000007639 printing Methods 0.000 abstract description 7
- 238000003756 stirring Methods 0.000 abstract description 2
- 231100000956 nontoxicity Toxicity 0.000 abstract 1
- 238000002791 soaking Methods 0.000 abstract 1
- 238000000034 method Methods 0.000 description 11
- 230000000694 effects Effects 0.000 description 9
- XEEYBQQBJWHFJM-UHFFFAOYSA-N iron Substances [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 8
- 238000002360 preparation method Methods 0.000 description 7
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 7
- 239000000047 product Substances 0.000 description 6
- 239000002699 waste material Substances 0.000 description 5
- 238000004042 decolorization Methods 0.000 description 4
- 238000010586 diagram Methods 0.000 description 4
- 239000000693 micelle Substances 0.000 description 3
- 235000010755 mineral Nutrition 0.000 description 3
- 238000004062 sedimentation Methods 0.000 description 3
- 238000005245 sintering Methods 0.000 description 3
- 238000001228 spectrum Methods 0.000 description 3
- 229910018084 Al-Fe Inorganic materials 0.000 description 2
- 229910018192 Al—Fe Inorganic materials 0.000 description 2
- BPQQTUXANYXVAA-UHFFFAOYSA-N Orthosilicate Chemical compound [O-][Si]([O-])([O-])[O-] BPQQTUXANYXVAA-UHFFFAOYSA-N 0.000 description 2
- 238000010306 acid treatment Methods 0.000 description 2
- VSCWAEJMTAWNJL-UHFFFAOYSA-K aluminium trichloride Chemical compound Cl[Al](Cl)Cl VSCWAEJMTAWNJL-UHFFFAOYSA-K 0.000 description 2
- 230000015271 coagulation Effects 0.000 description 2
- 238000005345 coagulation Methods 0.000 description 2
- 238000005265 energy consumption Methods 0.000 description 2
- 238000002474 experimental method Methods 0.000 description 2
- 239000011790 ferrous sulphate Substances 0.000 description 2
- 235000003891 ferrous sulphate Nutrition 0.000 description 2
- 238000005189 flocculation Methods 0.000 description 2
- 230000016615 flocculation Effects 0.000 description 2
- BAUYGSIQEAFULO-UHFFFAOYSA-L iron(2+) sulfate (anhydrous) Chemical compound [Fe+2].[O-]S([O-])(=O)=O BAUYGSIQEAFULO-UHFFFAOYSA-L 0.000 description 2
- 229910000359 iron(II) sulfate Inorganic materials 0.000 description 2
- 239000010808 liquid waste Substances 0.000 description 2
- 239000011777 magnesium Substances 0.000 description 2
- 238000002156 mixing Methods 0.000 description 2
- BHPQYMZQTOCNFJ-UHFFFAOYSA-N Calcium cation Chemical compound [Ca+2] BHPQYMZQTOCNFJ-UHFFFAOYSA-N 0.000 description 1
- VEXZGXHMUGYJMC-UHFFFAOYSA-M Chloride anion Chemical compound [Cl-] VEXZGXHMUGYJMC-UHFFFAOYSA-M 0.000 description 1
- FYYHWMGAXLPEAU-UHFFFAOYSA-N Magnesium Chemical compound [Mg] FYYHWMGAXLPEAU-UHFFFAOYSA-N 0.000 description 1
- DPDMMXDBJGCCQC-UHFFFAOYSA-N [Na].[Cl] Chemical compound [Na].[Cl] DPDMMXDBJGCCQC-UHFFFAOYSA-N 0.000 description 1
- 238000010521 absorption reaction Methods 0.000 description 1
- 230000002378 acidificating effect Effects 0.000 description 1
- 159000000013 aluminium salts Chemical class 0.000 description 1
- 229910000329 aluminium sulfate Inorganic materials 0.000 description 1
- 239000002585 base Substances 0.000 description 1
- 229910001570 bauxite Inorganic materials 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 239000011575 calcium Substances 0.000 description 1
- 229910001424 calcium ion Inorganic materials 0.000 description 1
- 159000000007 calcium salts Chemical class 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 230000001112 coagulating effect Effects 0.000 description 1
- 238000013329 compounding Methods 0.000 description 1
- 239000000470 constituent Substances 0.000 description 1
- 238000009792 diffusion process Methods 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 239000000975 dye Substances 0.000 description 1
- 239000000835 fiber Substances 0.000 description 1
- 229910010272 inorganic material Inorganic materials 0.000 description 1
- 239000011147 inorganic material Substances 0.000 description 1
- 229910017053 inorganic salt Inorganic materials 0.000 description 1
- 229910052749 magnesium Inorganic materials 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 229910044991 metal oxide Inorganic materials 0.000 description 1
- 150000004706 metal oxides Chemical class 0.000 description 1
- 238000000465 moulding Methods 0.000 description 1
- 239000011368 organic material Substances 0.000 description 1
- 230000020477 pH reduction Effects 0.000 description 1
- 229920000642 polymer Polymers 0.000 description 1
- 150000003839 salts Chemical class 0.000 description 1
- 238000012216 screening Methods 0.000 description 1
- 239000013049 sediment Substances 0.000 description 1
- 239000002893 slag Substances 0.000 description 1
- 239000002002 slurry Substances 0.000 description 1
- 239000002910 solid waste Substances 0.000 description 1
- 238000001179 sorption measurement Methods 0.000 description 1
- 241000894007 species Species 0.000 description 1
- 239000001117 sulphuric acid Substances 0.000 description 1
- 235000011149 sulphuric acid Nutrition 0.000 description 1
- 239000006228 supernatant Substances 0.000 description 1
- 238000005406 washing Methods 0.000 description 1
- 238000004065 wastewater treatment Methods 0.000 description 1
- 150000003751 zinc Chemical class 0.000 description 1
Images
Landscapes
- Separation Of Suspended Particles By Flocculating Agents (AREA)
Abstract
The present invention relates to a coagulant for treating printing and dyeing waste water and a production process thereof. Diluted acid solution which accounts for 22 to 31% of the total weight of the coagulant is added with flyash which accounts for 61 to 74% of the total weight of the coagulant, acid soaking reaction is carried out in the state of stirring, and after cooling for six to eight hours and metal ions are completely separated by acid, inorganic re-compounded component which accounts for 2% to 10% of the total weight of the coagulant is added to form the required coagulant. The coagulant has the advantages of low price, high efficiency and no toxicity, and the production process has the advantages of simple manufacture technology, convenient operation, low product cost and simple and applicable production method.
Description
Technical field
The present invention relates to a kind of purifying liquid waste, especially relate to a kind of coagulating agent and production method thereof of treatment of dyeing and printing with coagulating agent and production method thereof.
Background technology
Dyeing waste water is mixed by the waste water of each workshop section's discharging in the printing and dyeing course of processing.Dyeing waste water has that the water yield is big, colourity is high, complicated component, organic content height, water quality and quantity change the characteristics that wait greatly.Its main component has dyestuff, slurry, fiber impurity and other organic and inorganic material.
At the characteristics of dyeing waste water, main at present employing coagulant sedimentation is as pretreated method.The coagulating agent that uses is based on aluminium salt and molysite two class inorganic coagulants.Recently, to handle the report of such waste water quite a few about zinc salt, magnesium salts and silicate coagulating agent and compounding coagulation agent.Though shortcomings such as these coagulating agent have their own characteristics each, and ubiquity processing cost height or COD and chroma removal rate are limited have limited it and have applied.Therefore, be badly in need of researching and developing dyeing water treatment coagulating agent inexpensive, efficient, wide spectrum.
Flyash is a kind of solid waste that produces in coal-fired process, and enormous amount is serious to the pollution and the harm of environment.Both at home and abroad all in the method for seeking suitable comprehensive utilization flyash.Flyash is made into to purify liquid waste with coagulating agent be a kind of technological method of turning waste into wealth.
Flyash is after suitable acid treatment, and the metal oxide that wherein contains is dissolved, and generates metal hydrate under certain condition, has the flocculation function; Undissolved silicate skeleton is vesicular structure, has stronger physics and chemisorption performance.Therefore, utilize flyash to be raw material, can make the fly ash base coagulating agent, can be used for the processing of various trade effluents, the clearance height of SS, colourity and the COD of waste water through certain processing.
At present, the general technology of the preparation flyash coagulating agent of bibliographical information is:
Flyash → screening → washing → oven dry → levigate powdery → dilute sulphuric acid lixiviate → flyash the coagulating agent of making
↑ ↑ ↑ oven dry
In (adding or do not add the bauxite slag) (adding or do not add solubility promoter the sodium-chlor) 〉=90 ℃ product flyash coagulating agent that obtains of high temperature, contain Al usually
2O
3, Fe
2O
3, SiO
2, CaO and MgO.Some patented technologies are improved on this technology basis for cooperating actual the use, as: ZL01128398.X has introduced a kind of method of utilizing flyash to produce inorganic Al-Fe polymerized coagulant.This method through sinter molding, adds two kinds of acid-responss with the batching of pre-dry forming, is modulated into finished product.Acidification reaction is kept Al
3+: SO
4 2-: Cl
-Molar concentration rate is all the time at 2: 6: 11.Whole process of production is complicated, and needs the pre-dry forming of batching sintering, and energy consumption is higher.Because this coagulating agent is a kind of inorganic Al-Fe polymerized thing, for the processing of strong basicity dyeing waste water, must regulate the pH value in advance, has increased running cost.Patent ZL200410026541.8, denomination of invention is a kind of treatment of dyeing wastewater coagulating agent and production method thereof.This invention is dissolved in mineral acid in proportion with molysite, magnesium salts and calcium salt, and makes finished product through the rotary kiln high temperature sintering.The effective constituent of finished product is FeO16.94-21.18%, Fe
2O
310.29-13.24%, MgO0.77-2.56%, CaO0.33-1.63%.This coagulating agent is a slightly acidic, need regulate the pH value during use.This coagulating agent raw material is an inorganic salts, is not flyash, and needs in preparation process through the rotary kiln high temperature sintering, and energy consumption is higher, so product price is also corresponding higher.
Summary of the invention
Technical problem to be solved by this invention is in order to overcome the problem that above-mentioned prior art exists, and is the coagulating agent of inexpensive, efficient, the wide spectrum that forms of feedstock production with flyash and provide a kind of;
Another object of the present invention provides a kind of preparation technology preparation method of above-mentioned coagulating agent simply and easily.
Technical scheme of the present invention is: a kind of coagulant for disposing dying waste water, its composition and weight percentage are: the flyash that accounts for coagulating agent gross weight 61-74%, account for the diluted acid of coagulating agent gross weight 22-31%, account for the inorganic composite composition of coagulating agent gross weight 2-10%; The weight percentage of its chemical composition is CaO 0.1-0.5%, MgO 5-10%, Fe
2O
30.1-8.8% (its water-soluble inorganic salt is in oxide compound), all the other for based on the impurity 40-60% of Si oxide (with SiO
2Meter).
Wherein said flyash is preferably flying dust.Described acid is mineral acid or its mixing acid, preferably sulfuric acid or hydrochloric acid, and its concentration is 2～4mol/L; Described inorganic being re-dubbed is divided into magnesium salts or the magnesium salts mixture with molysite; The weight proportion of magnesium salts and molysite is 4: 1～1: 2 in the preferred inorganic composite composition.
Composite magnesium salts and molysite in this coagulating agent.Magnesium salts and molysite have increased the intensity of gegenion in the solution, have reduced the thickness of diffusion layer, reduce effectively or have eliminated the ξDian Wei of suspension micelle in the water, make its micelle loss of stability.Simultaneously, fly ash grain has formed many grooves and hole on the surface after acid treatment, can adsorb these and take off steady micelle and other charge specieses.In treating processes, the fly ash grain in the coagulating agent is scattered in the waste water.Because the adsorption of flyash, many complex compounds and high molecular polymer have formed bigger suspensoid in the middle of fly ash grain is wrapped in.When stopping to stir, these include suspensoids of fly ash grain because quality is bigger, rapidly sedimentation, and reduced the volume of sediment.Water soluble magnesium, iron, calcium ion play the complex coagulation effect to the impurity in the waste water, and insoluble flyash particulate plays absorption, helps heavy effect the throw out in the waste water.Their synergy makes that this coagulating agent is effective to treatment of dyeing wastewater, speed is fast.
Coagulating agent of the present invention is a kind of novel composite coagulant, and outward appearance is the tawny suspension liquid, contains Mg
2+, Fe
3+, Ca
2+Etc. multiple inorganic components, pH value 5～6.Similar coagulating agent with other of this product such as ferrous sulfate, sal epsom are compared, and have that preparation technology is simple, easy to operate, the percent of decolourization height of treatment of dyeing and printing, COD clearance are big, the obvious advantage such as reduction of cost for wastewater treatment.Its raw materials cost is dozens of yuan/ton only.
The present invention also provides the production method of above-mentioned coagulant for disposing dying waste water, and its step comprises:
A. in an acid proof reactor, add the dilute acid soln that accounts for coagulating agent gross weight 22-31%, under whipped state, add the flyash that accounts for coagulating agent gross weight 61-74%, carry out acid-leaching reaction;
B. with above-mentioned solution cooling 6-8 hour, treat that metal ion is gone out by acidleach fully after, add the inorganic composite composition that accounts for coagulating agent gross weight 2-10% again, obtain the tawny suspension liquid and be required coagulating agent.
Wherein, the flyash in the steps A is preferably flying dust; Acid is mineral acid or its mixing acid, preferably sulfuric acid or hydrochloric acid, and its concentration is 2～4mol/L; Inorganic among the step B is re-dubbed and is divided into magnesium salts or the magnesium salts mixture with molysite, and magnesium salts is 4: 1～1: 2 with the weight proportion of molysite in the preferred inorganic composite composition.
Coagulating agent preparation technology of the present invention is simple, with low cost, the treatment of wastes with processes of wastes against one another, and to dyeing waste water (comprising waste water of basic printing and dyeing) good decolorizing effect, COD clearance height, running cost is lower.This coagulating agent can be directly used in 200～10000 times of colourities, the dyeing waste water that the pH value is not limit.
Beneficial effect
1. the invention provides a kind of coagulating agent inexpensive, efficient, wide spectrum and administer dyeing waste water.
2. this coagulating agent is effective to treatment of dyeing wastewater, and the flco of generation is big, and settling velocity is fast, and running cost is low.
3. add inorganic composite composition in this coagulating agent, strengthened the effect of flocculation.
4. coagulating agent preparation method provided by the invention utilizes depleted flyash to activate through diluted acid at normal temperatures and pressures to make simple, the easy to operate and treatment of wastes with processes of wastes against one another of manufacture craft.
Description of drawings
Fig. 1 is the influence synoptic diagram of different coagulants of the present invention to clearance.The coagulating agent 2.FeSO that 1. the present invention make among the figure
4, 3.FeCl
3, 4.AlCl
3, 5.MgSO
4, COD clearance, ■ percent of decolourization.
The coagulating agent that Fig. 2 makes for the present invention and the cost comparison diagram of other coagulating agent.1. the present invention make coagulating agent 2.FeSO among the figure
4, 3.FeCl
3, 4.AlCl
3, 5.MgSO
4The longitudinal axis is represented cost of water treatment/unit per ton.
The coagulating agent that Fig. 3 makes for the present invention and the treatment effect comparison diagram of other coagulating agent.Among the figure 1: the coagulating agent that the present invention makes, 2:FeSO
4, 3:AlCl
3, 4:FeCl
3, 5:MgSO
4, COD clearance, ■ percent of decolourization.
The coagulating agent that Fig. 4 makes for the present invention and the cost comparison diagram of other coagulating agent.Among the figure 1: the coagulating agent that the present invention makes, 2:FeSO
4, 3:AlCl
3, 4:FeCl
3, 5:MgSO
4, the longitudinal axis is represented cost of water treatment/unit per ton.
Embodiment
1. what this experiment was adopted is the dyeing waste water of Nantong printing and dyeing mill, and color is a red-purple, and the pH value is between 8～9, and about COD360mg/L, about 200 times of colourity contains a small amount of suspended substance.Add an amount of ferrous sulfate, sal epsom respectively, aluminum chloride, the coagulating agent that iron(ic) chloride and the present invention make, control optimum reaction condition separately carries out coagulating sedimentation, gets supernatant liquor and measures its COD value and colourity, and treatment effect is as shown in Figures 1 and 2.Under the suitable situation of treatment effect, the cost of the coagulating agent TREATMENT OF DYEING WASTEWATER WITH that utilization the present invention makes is much smaller with respect to other coagulating agent, can significantly reduce investment and working cost.
Do not add composite composition and the contrast of the composite composition that adds different mass in the coagulating agent that table 1 makes for the present invention to this treatment of dyeing wastewater efficient.
Table 1
2. the process object of this experiment is the dyeing waste-water of Nantong printing and dyeing mill, and its color is a black, and colourity is about 10000 times, COD value 1150mg/L, pH value about 6.Contain a small amount of suspended substance in the waste water.The coagulating agent, the FeSO that select for use the present invention to make
4, FeCl
3, AlCl
3And MgSO
4Five kinds of coagulating agent are handled this dyeing waste-water, are that the index of treatment effect compares with COD clearance and percent of decolourization, and experimental result is seen Fig. 3 and Fig. 4.This coagulating agent not only is better than other similar coagulating agent from effect, and has also shown superiority on cost.
Do not add composite composition and the contrast of the composite composition that adds different mass in the coagulating agent that table 2 makes for the present invention to this treatment of dyeing wastewater efficient.
Table 2
Claims (5)
1. coagulant for disposing dying waste water, it is characterized in that: its raw material is formed and weight percentage is respectively the flyash that accounts for coagulating agent raw material total amount weight percentage 61-74%, accounting for coagulating agent raw material total amount weight percentage 22-31% concentration is the acid solution of 2～4mol/L, account for the inorganic composite composition of coagulating agent raw material total amount weight percentage 2-10%, and prepare by following steps: A. is in the acid solution of 22-31% accounting for coagulating agent raw material total amount weight percentage, add under whipped state that to account for coagulating agent raw material total amount weight percentage be 61-74% flyash, carry out acid-leaching reaction; B. with above-mentioned solution cooling 6-8 hour, treat that metal ion is gone out by acidleach fully after, add again that to account for coagulating agent raw material total amount weight percentage be the inorganic composite composition of 2-10%, obtain the tawny suspension liquid of pH 5-6, be required coagulating agent; The oxide compound that its chemical composition is pressed in the composite composition of water-soluble inorganic calculates, and its weight percentage is respectively CaO 0.1-0.5%, MgO 5-10%, Fe
2O
30.1-8.8%, all the other are main impurity for Si oxide, with SiO
2Be calculated as 40-60%; Wherein said inorganic composite composition is magnesium salts or the magnesium salts mixture with molysite.
2. coagulating agent according to claim 1 is characterized in that flyash is flying dust.
3. coagulating agent according to claim 1 is characterized in that described acid solution is mineral acid or its mixed acid solution.
4. coagulating agent according to claim 3 is characterized in that described acid solution is sulfuric acid or hydrochloric acid soln.
5. coagulating agent according to claim 1 is characterized in that magnesium salts in the inorganic composite composition is 4: 1～1: 2 with the weight proportion of molysite.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB2005100940554A CN100387532C (en) | 2005-08-26 | 2005-08-26 | Coagulant for disposing dying waste water and its production method |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB2005100940554A CN100387532C (en) | 2005-08-26 | 2005-08-26 | Coagulant for disposing dying waste water and its production method |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN1762848A CN1762848A (en) | 2006-04-26 |
| CN100387532C true CN100387532C (en) | 2008-05-14 |
Family
ID=36747212
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CNB2005100940554A Expired - Fee Related CN100387532C (en) | 2005-08-26 | 2005-08-26 | Coagulant for disposing dying waste water and its production method |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN100387532C (en) |
Families Citing this family (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101638259B (en) * | 2009-09-02 | 2011-11-09 | 济南大学 | Method for preparing synthesized high iron-based silicon compound high-molecular coagulant adopting flyash extract |
| CN102786123A (en) * | 2011-05-20 | 2012-11-21 | 上海丰信环保科技有限公司 | Preparation method of composite flocculating agent |
| CN104402102B (en) * | 2014-12-09 | 2016-10-05 | 浙江省环境保护科学设计研究院 | A kind of dyeing waste water strenuous primary treatment coagulant and preparation method thereof |
| CN108238669A (en) * | 2016-12-27 | 2018-07-03 | 海门市源美美术图案设计有限公司 | It is a kind of for compound coagulant for denitrogenating and preparation method thereof |
| CN111807576A (en) * | 2020-07-21 | 2020-10-23 | 常熟理工学院 | Method for treating domestic garbage leachate by using domestic garbage incineration fly ash |
| CN115043452B (en) * | 2022-08-10 | 2023-05-23 | 江苏莱通环境科技有限公司 | Sewage treatment agent adding method and device based on effluent color |
Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4397742A (en) * | 1979-06-20 | 1983-08-09 | Minnick L John | Composition and method combining fluidized bed residue with scrubber sludge |
| CN87103664A (en) * | 1987-05-15 | 1987-12-02 | 南京大学 | Synthetic glass factory cyanide wastewater treatment process method |
| CN1035623A (en) * | 1989-03-02 | 1989-09-20 | 周天保 | Produce the method for composite flocculation agent with the cinder powder |
| CN1091724A (en) * | 1993-03-05 | 1994-09-07 | 马桂荣 | Handle the method for (plating) chromate waste water with silicate material |
| CN1160682A (en) * | 1996-04-01 | 1997-10-01 | 国家海洋局海洋环境保护研究所 | Composite coagulant for water treatment and its preparation process |
| CN1183384A (en) * | 1996-11-27 | 1998-06-03 | 黄卫平 | Paper-making waste water treating agent, its use and process for treatment of papermaking waste water therewith |
-
2005
- 2005-08-26 CN CNB2005100940554A patent/CN100387532C/en not_active Expired - Fee Related
Patent Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4397742A (en) * | 1979-06-20 | 1983-08-09 | Minnick L John | Composition and method combining fluidized bed residue with scrubber sludge |
| CN87103664A (en) * | 1987-05-15 | 1987-12-02 | 南京大学 | Synthetic glass factory cyanide wastewater treatment process method |
| CN1035623A (en) * | 1989-03-02 | 1989-09-20 | 周天保 | Produce the method for composite flocculation agent with the cinder powder |
| CN1091724A (en) * | 1993-03-05 | 1994-09-07 | 马桂荣 | Handle the method for (plating) chromate waste water with silicate material |
| CN1160682A (en) * | 1996-04-01 | 1997-10-01 | 国家海洋局海洋环境保护研究所 | Composite coagulant for water treatment and its preparation process |
| CN1183384A (en) * | 1996-11-27 | 1998-06-03 | 黄卫平 | Paper-making waste water treating agent, its use and process for treatment of papermaking waste water therewith |
Non-Patent Citations (4)
| Title |
|---|
| 粉煤灰处理印染废水. 贾毅竹.内蒙古环境保护，第12卷第1期. 2000 |
| 粉煤灰处理印染废水. 贾毅竹.内蒙古环境保护，第12卷第1期. 2000 * |
| 粉煤灰漂珠代替活性碳处理废水的技术研究. 李尉卿，苏彩丽，董中强.粉煤灰，第5期. 2000 |
| 粉煤灰漂珠代替活性碳处理废水的技术研究. 李尉卿，苏彩丽，董中强.粉煤灰，第5期. 2000 * |
Also Published As
| Publication number | Publication date |
|---|---|
| CN1762848A (en) | 2006-04-26 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| Sun et al. | Effect of silicon dose on preparation and coagulation performance of poly-ferric-aluminum-silicate-sulfate from oil shale ash | |
| CN100387532C (en) | Coagulant for disposing dying waste water and its production method | |
| CN100542976C (en) | Method with flyash and kaolin production compound aluminium silicate polymer ferric flocculant | |
| CN107311277B (en) | Nanometer medicament for simultaneously removing arsenic, phosphorus and fluorine in water and preparation method thereof | |
| CN1830823B (en) | Treatment agent for textile dyeing waste water | |
| CN108083345A (en) | A kind of method that polymeric aluminum sulfate silicate iron composite flocculation agent is prepared using red mud waste material | |
| CN101941755B (en) | Modified coal ash, preparation method thereof and method thereof for treating humic acid | |
| CN101597102A (en) | A kind of preparation method who is used for the magnetic flocculant of magnetic separation method water processing technique | |
| CN102674513B (en) | Composite medicinal preparation for biochemical effluent deep treatment of sewage plant | |
| CN102942237A (en) | Preparation method for water purifier capable of synchronously removing ammonia nitrogen and phosphorus in waste water | |
| CN106745624A (en) | A kind of inorganic-organic hybrid flocculation material and preparation method thereof | |
| CN101003390A (en) | Method for preparing flocculant of ferric chloride of polysilicon acid | |
| CN102115234A (en) | Preparation method of flocculant capable of removing phosphate from red mud | |
| CN105854784A (en) | Method for preparing environmental protection material used for sewage treatment by reforming metallurgical dregs | |
| CN101773817A (en) | Composite absorption material for wastewater treatment and preparation method thereof | |
| CN113860458B (en) | Composite chelating agent and preparation method and application thereof | |
| Li et al. | Synthesis of magnesium-modified ceramsite from iron tailings as efficient adsorbent for phosphorus removal | |
| CN102689906A (en) | Method for preparing polysilicate aluminum ferric chloride by using aluminum foil acid and ferrous acid | |
| CN107162150A (en) | Canal reactor efficient water-purifying agent and preparation method thereof | |
| CN104310553A (en) | Resource utilization method of blast furnace dust | |
| CN111921491A (en) | Preparation method of magnetic activated carbon and method for enhancing and improving secondary effluent efficiency of coagulation treatment based on magnetic activated carbon | |
| JP2001347104A (en) | Powdery decontaminant and method of decontaminating clean water and waste water | |
| CN100447080C (en) | Method for preparing ferric sulfate of polymerized silica by using metallurgy dregs | |
| CN109319896A (en) | The method for preparing flocculant with flyash and vanadium titano-magnetite | |
| CN114853109A (en) | Deep defluorination medicament and preparation method and use method thereof |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| EE01 | Entry into force of recordation of patent licensing contract |
Assignee: NJTECH ENVIRONMENT TECHNOLOGY Co.,Ltd. Assignor: Nanjing University of Technology Contract record no.: 2012320000195 Denomination of invention: Coagulant for treating printing and dyeing wastewater and production method thereof Granted publication date: 20080514 License type: Exclusive License Open date: 20060426 Record date: 20120313 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20080514 Termination date: 20210826 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |