CN217323729U - System for ferric phosphate contains full element resourceful treatment of ammonia nitrogen waste water - Google Patents
System for ferric phosphate contains full element resourceful treatment of ammonia nitrogen waste water Download PDFInfo
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- CN217323729U CN217323729U CN202121524026.8U CN202121524026U CN217323729U CN 217323729 U CN217323729 U CN 217323729U CN 202121524026 U CN202121524026 U CN 202121524026U CN 217323729 U CN217323729 U CN 217323729U
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Abstract
The utility model provides a system for iron phosphate ammonia nitrogen containing wastewater full-element resource treatment, which comprises a wastewater storage tank, a first reaction device, a first filtering device, a second reaction device, a second filtering device, a third reaction device, a third filtering device, a stripping deamination device, a fourth reaction device, a fourth filtering device, a fifth reaction device, a fifth filtering device, a concentration device and a pH adjusting device; the utility model discloses waste water adds the ammonia earlier and adjusts pH, unnecessary iron in the waste water, impurity such as impurity manganese, zinc that the raw materials brought deposits with the mode of alkaline phosphate or hydroxide, avoids these impurity to influence the quality of calcium sulfate.
Description
Technical Field
The utility model relates to an industrial wastewater treatment field, concretely relates to ferric phosphate contains full element resourceful treatment's of ammonia nitrogen waste water system.
Background
The lithium ion battery is a high-energy battery which can achieve the charging and discharging effect by circularly and repeatedly inserting and extracting lithium ions in the isomorphic interior between a positive electrode material and a negative electrode material with a layered structure. The lithium ion battery mainly comprises a positive electrode, a negative electrode, a diaphragm, electrolyte and a conductive current collector. The anode material mainly comprises lithium cobaltate, nickel-cobalt-manganese or nickel-cobalt-aluminum ternary, lithium manganate, lithium iron phosphate and doped compounds thereof.
The preparation process of the precursor ferric phosphate of the lithium iron phosphate mainly comprises a coprecipitation method, a hydrothermal method and the like, wherein the coprecipitation method is widely applied. The coprecipitation method is to dissolve an iron source and a phosphorus source, add other compounds, precipitate the mixture with hydrated iron phosphate, and then wash, dry and calcine the mixture to obtain an iron phosphate product. In the process of preparing the iron phosphate, a large amount of high-concentration wastewater containing ammonia, phosphorus and sulfur is generated, in the prior production technology, the effective components of the iron phosphate mother liquor cannot be recovered, and the pollutants such as phosphorus, ammonia and the like in the mother liquor need to be effectively treated by adopting a complex and expensive process, so that the serious resource waste is caused, and the production cost and the environmental protection pressure of enterprises are increased.
Therefore, improvements in the prior art are needed.
SUMMERY OF THE UTILITY MODEL
The to-be-solved technical problem of the utility model is to provide an efficient ferric phosphate contains full element resourceful treatment's of ammonia nitrogen waste water system.
In order to solve the technical problem, the utility model provides a system for iron phosphate ammonia nitrogen containing wastewater full element resource treatment, which comprises a wastewater storage tank, a first reaction device, a first filtering device, a second reaction device, a second filtering device, a third reaction device, a third filtering device, a steam stripping deamination device, a fourth reaction device, a fourth filtering device, a fifth reaction device, a fifth filtering device, a concentration device and a pH adjusting device;
the waste water storage tank is connected with an inlet of the first reaction device;
the inlet of the first reaction device is connected with the inlet of the first filtering device;
the solution outlet of the first filtering device and the inlet of the second reaction device;
the outlet of the second reaction device is connected with the inlet of the second filtering device;
the solution outlet of the second filtering device is connected with the inlet of the third reaction device;
the outlet of the third reaction device is connected with the inlet of the third filtering device;
the solid outlet of the third filtering device is connected with the inlet of the fourth reaction device;
the outlet of the fourth reaction device is connected with the inlet of the fourth filtering device;
the solution outlet of the fourth filtering device is connected with the inlet of the fifth reaction device;
the outlet of the fifth reaction device is connected with the inlet of the fifth filtering device;
the solution outlet of the third filtering device and the solution outlet of the fifth filtering device are both connected with the inlet of the stripping deamination device;
and the outlet at the bottom of the stripping deamination device is respectively connected with the inlet of the concentration device and the inlet of the pH adjusting device.
As to the utility model relates to an improvement of iron phosphate contains full element resourceful treatment's of ammonia nitrogen waste water system:
the waste water storage tank is used for storing iron phosphate waste water;
the first reaction device, the second reaction device, the third reaction device, the fourth reaction device and the fifth reaction device are used for wastewater reaction, and can be one or more of a kettle type stirrer, a tower type stirrer and a horizontal multistage stirrer;
the first filtering device, the second filtering device, the third filtering device, the fourth filtering device and the fifth filtering device are used for filtering and can be one or more of a plate-and-frame filter press, a centrifugal machine, a vacuum belt filter and a disc dehydrator;
the stripping deamination device is used for recovering ammonia water by stripping deamination, and the main equipment is the combination of equipment such as a stripping rectifying tower, a condenser and the like;
the concentration device is used for concentrating the sodium sulfate and miscellaneous salts in the wastewater and the evaporative crystallization wastewater;
the pH adjusting device is used for adjusting the pH value of the wastewater and can be one of a kettle type stirrer, a tubular reactor, a tower type stirrer and a multistage series stirrer.
The utility model relates to a system and method for iron phosphate ammonia nitrogen wastewater full-element resource treatment, which has the technical advantages that:
1) firstly adding ammonia water into the wastewater to adjust the pH value, and precipitating impurities such as redundant iron in the wastewater and impurities such as manganese, zinc and the like brought by raw materials in the form of alkaline phosphate or hydroxide, so as to avoid the influence of the impurities on the quality of calcium sulfate;
2) calcium hydroxide is used for fractional precipitation to respectively obtain calcium hydrophosphate and calcium sulfate dihydrate, phosphorus and sulfur in the wastewater are respectively recovered, and various elements in the wastewater are utilized to the maximum benefit;
3) the by-product calcium sulfate dihydrate is purified, so that magnesium, phosphorus and ammonia in the calcium sulfate are removed, and the problem that the calcium sulfate cannot be recycled is avoided;
4) ammonia in the wastewater is recycled into 20% ammonia water by utilizing stripping deamination, so that the benefit of the ammonia element is maximized;
the steps realize the recycling of all elements of phosphorus, sulfur and ammonia in the wastewater, and have great social and economic benefits.
Drawings
The following describes the present invention in further detail with reference to the accompanying drawings.
Figure 1 is the module schematic diagram of the system for the total-element resource treatment of the iron phosphate ammonia nitrogen-containing wastewater.
Detailed Description
The invention will be further described with reference to specific examples, but the scope of the invention is not limited thereto.
Embodiment 1, a system for iron phosphate ammonia nitrogen containing wastewater full-element resource treatment, as shown in fig. 1, includes a wastewater storage tank 4, a first reaction device 5, a first filtering device 6, a second reaction device 7, a second filtering device 8, a third reaction device 9, a third filtering device 10, a stripping deamination device 17, a fourth reaction device 11, a fourth filtering device 13, a fifth reaction device 15, a fifth filtering device 16, a concentration device 18, and a pH adjusting device 19.
The waste water storage tank 4 is used for storing iron phosphate waste water;
the first reaction device 5, the second reaction device 7, the third reaction device 9, the fourth reaction device 11 and the fifth reaction device 15 are used for wastewater reaction, and can be one or more of a kettle type stirrer, a tower type stirrer and a horizontal multi-stage stirrer.
The first filtering device 6, the second filtering device 8, the third filtering device 10, the fourth filtering device 13 and the fifth filtering device 16 are used for filtering, and can be one or more of a plate-and-frame filter press, a centrifugal machine, a vacuum belt filter and a disc dehydrator.
The stripping deamination device 17 is used for stripping deamination to recover ammonia water, and the main equipment is a combination of equipment such as a stripping rectifying tower, a condenser and the like.
The concentration device 18 is used for concentrating the sodium sulfate and miscellaneous salts in the wastewater and the evaporative crystallization wastewater;
the pH adjusting device 19 is used for adjusting the pH value of the wastewater, and can be one of a kettle type stirrer, a tubular reactor, a tower type stirrer or a multi-stage series stirrer.
The connection relationship among all devices of a system for iron phosphate ammonia nitrogen-containing wastewater full-element resource treatment is as follows:
the waste water storage tank 4 is connected with the inlet of the first reaction device 5;
the inlet of the first reaction device 5 is connected with the inlet of the first filtering device 6;
a solution outlet of the first filtering device 6 and an inlet of the second reaction device 7;
the outlet of the second reaction device 7 is connected with the inlet of a second filtering device 8;
the solution outlet of the second filtering device 8 is connected with the inlet of the third reaction device 9;
the outlet of the third reaction device 9 is connected with the inlet of a third filtering device 10;
the solid outlet of the third filtering device 10 is connected with the inlet of the fourth reaction device 11;
the outlet of the fourth reaction device 11 is connected with the inlet of a fourth filtering device 13;
the solution outlet of the fourth filtering device 13 is connected with the inlet of the fifth reaction device 15;
the outlet of the fifth reaction device 15 is connected with the inlet of a fifth filtering device 16;
the solution outlet of the third filtering device 10 and the solution outlet of the fifth filtering device 16 are both connected with the inlet of a stripping deamination device 17;
the outlet at the bottom of the stripping deamination device 17 is respectively connected with the inlet of a concentration device 18 and the inlet of a pH adjusting device 19.
A method for the total-element resource treatment of iron phosphate ammonia nitrogen-containing wastewater comprises the following steps:
1) adding the iron phosphate wastewater in the wastewater storage tank 4 into a first reaction device 5, adding ammonia water with the mass concentration of 20%, adjusting the pH value to 6-8, and carrying out the steps at normal temperature and normal pressure; iron ions, manganese ions and other heavy metal ions in the iron phosphate wastewater are precipitated in the form of alkaline iron phosphate, manganese phosphate or hydroxide, respectively, and then filtered in a first filtering device 6 to remove impurities in the wastewater.
2) Adding the iron phosphate wastewater filtrate obtained by filtering in the first filtering device 6 into a second reaction device 7, adding a calcium hydroxide solution (with the mass concentration of 10-30%) or a calcium hydroxide solid (with the content of 90-98%), adjusting the pH value to be 8-10, and carrying out the reaction at normal temperature and normal pressure to separate out a calcium hydrophosphate solid; then filtered in a second filtering device 8, and the filter cake is dried and sold or used for preparing phosphoric acid.
3) Adding the iron phosphate wastewater filtrate obtained by filtering in the second filtering device 8 into a third reaction device 9, adding a calcium hydroxide solution (with the mass concentration of 10-30%) or a calcium hydroxide solid (with the content of 90-98%), adjusting the pH value to be 11.5-12.5, and reacting at normal temperature and normal pressure to separate out calcium sulfate dihydrate and other magnesium hydroxide and calcium phosphate impurities; and then filtered in the third filtering device 10.
4) Slurrying a filter cake obtained by filtering in the third filtering device 10, adding the slurried filter cake into a fourth reaction device 11, adding sulfuric acid with the mass concentration of 1-25% or iron phosphate acidic wastewater (which can be selected alternatively) in an iron phosphate wastewater storage tank 4, adjusting the pH value of the slurry to be 2-5, and reacting at normal temperature and normal pressure; then re-filtering in a fourth filtering device 13, wherein the filtered filter cake is purified calcium sulfate dihydrate which is sold or post-treated for preparing gypsum or cement.
5) Adding the iron phosphate wastewater filtrate obtained by filtering in the fourth filtering device 13 into a fifth reaction device 15, adding a calcium hydroxide solution (with the mass concentration of 10-30%) or a calcium hydroxide solid (with the content of 90-98%), and adjusting the pH value to be 11.5-12.5; then filtered in a fifth filter device 16, and the filter cake after filtration is a mixture of calcium sulfate dihydrate and magnesium hydroxide, and is treated externally.
6) Mixing the alkaline wastewater obtained by filtering after the reaction in the third filtering device 10 and the fifth filtering device 16 (the wastewater contains 10-20g/L ammonia, a small amount of dissolved calcium sulfate and calcium hydroxide), adding the alkaline wastewater into a stripping deamination device 17 together for stripping deamination, recovering 15-20% ammonia water, wherein the ammonia nitrogen content in the deaminated wastewater is lower than 15 mg/L.
7) The deamination waste water obtained by the stripping deamination device 17 can be treated by one of the following two schemes:
the first scheme is as follows: adding a sodium carbonate solution into the deamination wastewater to obtain calcium, then adding the calcium into a concentration device 18 to perform membrane concentration, and performing evaporative crystallization to obtain sodium sulfate and a small amount of miscellaneous salts, thereby realizing zero discharge of wastewater;
scheme II: adding the deamination wastewater into a pH adjusting device 19, adding sulfuric acid or hydrochloric acid, adjusting the pH to be neutral, and discharging after reaching the standard. Wherein the mass concentration of the added sulfuric acid is 5-98%, and the mass concentration of the added hydrochloric acid is 5-31%.
Finally, it is also noted that the above-mentioned list is only a few specific embodiments of the present invention. Obviously, the present invention is not limited to the above embodiments, and many modifications are possible. All modifications which can be derived or suggested by the person skilled in the art from the disclosure of the invention should be considered as within the scope of the invention.
Claims (2)
1. The utility model provides a system for ferric phosphate contains full element resourceful treatment of ammonia nitrogen waste water which characterized in that: comprises a waste water storage tank (4), a first reaction device (5), a first filtering device (6), a second reaction device (7), a second filtering device (8), a third reaction device (9), a third filtering device (10), a stripping deamination device (17), a fourth reaction device (11), a fourth filtering device (13), a fifth reaction device (15), a fifth filtering device (16), a concentration device (18) and a pH adjusting device (19);
the wastewater storage tank (4) is connected with an inlet of the first reaction device (5);
the inlet of the first reaction device (5) is connected with the inlet of the first filtering device (6);
the solution outlet of the first filtering device (6) and the inlet of the second reaction device (7);
the outlet of the second reaction device (7) is connected with the inlet of a second filtering device (8);
the solution outlet of the second filtering device (8) is connected with the inlet of a third reaction device (9);
the outlet of the third reaction device (9) is connected with the inlet of a third filtering device (10);
the solid outlet of the third filtering device (10) is connected with the inlet of the fourth reaction device (11);
the outlet of the fourth reaction device (11) is connected with the inlet of a fourth filtering device (13);
the solution outlet of the fourth filtering device (13) is connected with the inlet of a fifth reaction device (15);
the outlet of the fifth reaction device (15) is connected with the inlet of a fifth filtering device (16);
the solution outlet of the third filtering device (10) and the solution outlet of the fifth filtering device (16) are both connected with the inlet of a stripping deamination device (17);
and the outlet at the bottom of the stripping deamination device (17) is respectively connected with the inlet of a concentration device (18) and the inlet of a pH adjusting device (19).
2. The system for the total-element resource treatment of the iron phosphate ammonia nitrogen-containing wastewater according to claim 1, which is characterized in that:
the waste water storage tank (4) is used for storing iron phosphate waste water;
the stripping deamination device (17) is used for recovering ammonia water by stripping deamination, and the main equipment is the combination of a stripping rectifying tower and a condenser;
the concentration device (18) is used for concentrating the sodium sulfate and miscellaneous salts in the wastewater and the evaporative crystallization wastewater;
the pH adjusting device (19) is used for adjusting the pH value of the wastewater.
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| CN202121524026.8U CN217323729U (en) | 2021-07-06 | 2021-07-06 | System for ferric phosphate contains full element resourceful treatment of ammonia nitrogen waste water |
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| CN202121524026.8U CN217323729U (en) | 2021-07-06 | 2021-07-06 | System for ferric phosphate contains full element resourceful treatment of ammonia nitrogen waste water |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
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| CN115806373A (en) * | 2023-02-06 | 2023-03-17 | 山东泰和科技股份有限公司 | Treatment method of iron phosphate production wastewater |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
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| CN115806373A (en) * | 2023-02-06 | 2023-03-17 | 山东泰和科技股份有限公司 | Treatment method of iron phosphate production wastewater |
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