CN215609028U - Safe processing device for scrapped sodium chlorite - Google Patents
Safe processing device for scrapped sodium chlorite Download PDFInfo
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- CN215609028U CN215609028U CN202121451897.1U CN202121451897U CN215609028U CN 215609028 U CN215609028 U CN 215609028U CN 202121451897 U CN202121451897 U CN 202121451897U CN 215609028 U CN215609028 U CN 215609028U
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Abstract
The utility model relates to a safe treatment device for scrapped sodium chlorite, which comprises a first dosing device, a second dosing device, a first reactor, a second reactor, a plate-frame filter press, an incineration treatment device and a sewage treatment device; the first dosing device is arranged on the first reactor and comprises a sodium chlorite inlet tank, a citric acid inlet tank and a pure water inlet tank; the lower part of the first reactor is connected with the upper part of the second reactor, the second dosing device is arranged on the second reactor and comprises a formaldehyde solution inlet tank, a potassium iodide solution inlet tank and a sodium hydroxide solution inlet tank; the lower part of the second reactor is connected with a plate frame filter press, the upper part of the plate frame filter press is connected with a sewage treatment device, and the lower part of the plate frame filter press is connected with an incineration disposal device; the upper parts of the first reactor and the second reactor are communicated with a gas treatment device.
Description
Technical Field
The utility model relates to the technical field of hazardous waste treatment, in particular to a safe treatment device for scrapped sodium chlorite.
Background
Sodium chlorite is a white or slightly yellowish green powder or granular crystal that is readily soluble in water and can cause explosions when contacted with organic matter. Has slight hygroscopicity and is stable at normal temperature. The anhydrous substance is not decomposed when heated to 350 ℃, and the hydrated sodium chlorite is decomposed when heated to 130-140 ℃. Is easily dissolved in water (34% at 5 ℃ and 46% at 30 ℃). The alkaline aqueous solution is stable to light, the acidic aqueous solution is explosively decomposed by light, and chlorine dioxide (or oxygen and chlorine) is released when the decomposition rate is higher as the acidity is higher.
Sodium chlorite is a high-efficiency oxidant and bleaching agent, and is mainly used for water treatment, pulp bleaching, deodorization, food preservation and other aspects. Sodium chlorite belongs to dangerous chemical, has strong oxidizing property, has 157 percent of theoretical available chlorine content of pure product, is contacted and mixed with wood chips, organic matters, sulfur, phosphorus, carbon and other combustible matters, and can cause explosion when being impacted and rubbed. Contact with the reducing substance can cause a violent reaction. Because sodium chlorite has high activity, the waste treatment difficulty is high, the treatment process has great potential safety hazard and has serious influence on ecological environment and human health, and no reference treatment device exists at present. Therefore, processes and apparatuses for solution pretreatment and multistage reaction have been studied to treat such hazardous wastes.
SUMMERY OF THE UTILITY MODEL
The utility model aims to provide a safe processing device for scrapped sodium chlorite, which is a safe and stable processing device for scrapped sodium chlorite and realizes the safe processing of sodium chlorite through a multistage reaction process by controlling a reaction system medicament. The method comprises the steps of reacting sodium chlorite and citric acid to generate sodium citrate, chlorine dioxide, sodium chloride and water, decomposing the sodium chlorite, reacting a formaldehyde aqueous solution with the chlorine dioxide, decomposing the chlorine dioxide into carbon dioxide, hydrogen chloride and water after two-step reaction, verifying whether the chlorine dioxide completely reacts by using a potassium iodide solution, further deeply treating the chlorine dioxide, and neutralizing by using sodium hydroxide to complete safe disposal of the sodium chlorite. The three wastes of the system are effectively collected and treated in the whole reaction process, so that the combined treatment device is safe in operating environment when the sodium chlorite is treated.
The technical scheme of the utility model is as follows: a safe treatment device for scrapped sodium chlorite comprises a first dosing device, a second dosing device, a first reactor, a second reactor, a plate frame filter press, an incineration treatment device and a sewage treatment device;
the first dosing device is arranged on the first reactor and comprises a sodium chlorite inlet tank, a citric acid inlet tank and a pure water inlet tank; the lower part of the first reactor is connected with the upper part of the second reactor, the second dosing device is arranged on the second reactor and comprises a formaldehyde solution inlet tank, a potassium iodide solution inlet tank and a sodium hydroxide solution inlet tank;
the lower part of the second reactor is connected with a plate frame filter press, the upper part of the plate frame filter press is connected with a sewage treatment device, and the lower part of the plate frame filter press is connected with an incineration disposal device;
the upper parts of the first reactor and the second reactor are communicated with a gas treatment device;
a first cooling water circulating device is arranged on the wall of the reaction kettle of the first reactor;
and a second cooling water circulating device is arranged on the wall of the reaction kettle of the second reactor.
Furthermore, the upper part of the first reactor is connected with a sodium chlorite inlet tank, a citric acid inlet tank and a pure water inlet tank, the upper part of the second reactor is provided with a formaldehyde solution inlet tank, a potassium iodide solution inlet tank and a sodium hydroxide solution inlet tank, and the lower part of the second reactor is connected with the middle part of the plate-and-frame filter press.
Furthermore, the gas treatment device comprises a gas condenser, a sulfuric acid solution absorber, a potassium iodide solution absorber, a sodium hydroxide absorber and a vacuum pump which are sequentially arranged along the gas discharge direction.
Furthermore, the first cooling water circulation device comprises a first cooling water circulation cavity arranged from the outer wall of the middle part of the first reactor to the outer wall of the lower part of the first reactor, a first cooling liquid inlet is arranged on the side wall of the first cooling water circulation cavity, and a first cooling liquid outlet is arranged at the bottom of the first cooling water circulation cavity.
Furthermore, the second cooling water circulation device comprises a second cooling water circulation cavity arranged from the outer wall of the middle part of the second reactor to the outer wall of the lower part of the second reactor, a second cooling liquid inlet is arranged on the side wall of the second cooling water circulation cavity, and a second cooling liquid outlet is arranged at the bottom of the second cooling water circulation cavity.
Furthermore, a first pump is arranged at the output end of the citric acid inlet tank, and the output end of the first pump is connected with the upper part of the first reactor; the bottom of the first reactor is provided with a first reactant outlet, the output end of the first reactant outlet is provided with a second pump, and the output end of the second pump is connected with the upper part of the second reactor; the bottom of the second reactor is provided with a second reactant outlet, the output end of the second reactant outlet is provided with a third pump, and the output end of the third pump is connected with the middle part of the plate frame filter press.
Still further, the first dosing device is arranged in the first reactor, and a thermometer is also arranged in the first reactor; the second medicine adding device is arranged in the second reactor, and a thermometer is also arranged in the second reactor.
Still further, a buffer tank is arranged in the gas treatment device.
The utility model discloses a safe processing method of scrapped sodium chlorite, with scrapped sodium chlorite as the main processing object, including the following steps:
1) firstly, dissolving and pretreating with pure water, pumping a citric acid solution into a reactor, reacting sodium chlorite and citric acid to form sodium citrate, chlorine dioxide, sodium chloride and water, decomposing chlorine dioxide in a system to form hydrogen chloride, carbon dioxide and water by using a formaldehyde solution as a reaction medicament in a mixed solution, and completely removing chlorine dioxide by using a potassium iodide solution under an acidic condition to form potassium iodide, potassium sulfate, iodine and water;
2) then adding sodium hydroxide to adjust the pH value to 8.0;
3) and finally, carrying out plate-and-frame filter pressing on the solid-liquid mixed solution, recycling the filtrate after evaporation desalination and biochemical treatment, and carrying out incineration treatment on the filter residue in a rotary kiln.
Furthermore, the safe processing method of the scrapped sodium chlorite of the utility model comprises the following steps:
1) reacting sodium chlorite with citric acid: adding scrapped sodium chlorite into a first reactor, adding pure water for dissolving, adding a citric acid solution through a first dosing device for reacting, and decomposing the sodium chlorite into sodium citrate, chlorine dioxide, sodium chloride and water;
2) reacting chlorine dioxide with formaldehyde: pumping the mixed solution treated in the step 1) into a second reactor, adding a formaldehyde solution into the second reactor through a second dosing device, and decomposing the chlorine dioxide through two steps of reaction to form carbon dioxide, hydrogen chloride and water; adding a potassium iodide solution through a second dosing device, on one hand, verifying whether chlorine dioxide completely reacts, on the other hand, completely reacting excessive chlorine dioxide, adding a sodium hydroxide solution into the solution after the reaction, and adjusting the pH value to about 8.0;
3) cooling: a large amount of heat energy is released in the reaction process of the step 1) and the step 2), and the temperature of a reaction system is controlled below 40 ℃ by cooling through circulating cooling water;
4) a solid-liquid separation system: carrying out plate-and-frame filter pressing on the mixed solution treated in the step 2), sending residues obtained after filter pressing to a rotary kiln for incineration treatment, and carrying out biochemical treatment on filter pressing wastewater after evaporation and desalination.
The utility model has the technical effects that: the utility model relates to a safe and stable treatment device for scrapped sodium chlorite, which realizes the safe treatment of sodium chlorite by controlling a reaction system medicament and a multistage reaction process. The technology of the utility model generates sodium citrate, chlorine dioxide, sodium chloride and water through the reaction of sodium chlorite and citric acid, realizes the decomposition of sodium chlorite, uses formaldehyde water solution to react with chlorine dioxide, decomposes the chlorine dioxide into carbon dioxide, hydrogen chloride and water after two-step reaction, finally adopts potassium iodide solution to verify whether the chlorine dioxide completely reacts, further deeply treats the chlorine dioxide, and finally adopts sodium hydroxide neutralization treatment to complete the safe disposal of the sodium chlorite. The three wastes of the system are effectively collected and treated in the whole reaction process, so that the combined treatment device is safe in operating environment when the sodium chlorite is treated.
Drawings
FIG. 1 is a diagram of the apparatus of the present invention.
Detailed Description
The waste sodium chlorite disposal device shown in fig. 1 comprises a first reactor 30 connected with a sodium chlorite storage tank, a second reactor 40, a plate frame filter press 50, an incineration treatment device 60, a sewage treatment device 70, and a gas treatment device 80 connected with the first reactor 30 and the second reactor 40, wherein the gas treatment device 80 comprises a gas condenser 81, a sulfuric acid solution absorber 82, a potassium iodide solution absorber 83, a sodium hydroxide absorber 84 and a vacuum pump 85 which are sequentially arranged along a gas discharge direction. Wherein, a pump is arranged in the scrapped sodium chlorite storage tank; a first dosing device 10 (a sodium chlorite inlet tank 11, a citric acid inlet tank 12 and a pure water inlet tank 13 are arranged inside the first reactor 30) and a thermometer can be arranged inside the first reactor 30; a second dosing device 20 (a formaldehyde solution inlet tank 21, a potassium iodide solution inlet tank 22 and a sodium hydroxide solution inlet tank 23 are arranged inside the second reactor 40) and a thermometer can be arranged inside the second reactor 40; a slurry pump is arranged in the plate-frame filter press 50; the gas processing apparatus 80 is provided therein with a buffer tank.
The utility model adopts the following technical scheme-a disposal device:
a safe sodium chlorite treatment device comprises a first dosing device 10, a second dosing device 20, a first reactor 30 (citric acid reaction), a second reactor 40 (formaldehyde reaction and potassium iodide reaction), a plate-frame filter press 50, an incineration disposal device 60, a sewage treatment device 70 and a gas treatment device 80.
The upper part of the first reactor 30 is connected with a sodium chlorite inlet tank 11, a citric acid inlet tank 12 and a pure water inlet tank 13, the lower part of the first reactor 30 is connected with the upper part of the second reactor 40, the upper part of the second reactor 40 is provided with a formaldehyde solution inlet tank 21, a potassium iodide solution inlet tank 22 and a sodium hydroxide solution inlet tank 23, the lower part of the second reactor 40 is connected with (the middle part of) a plate frame pressure filter 50, the upper parts of the first reactor 30 and the second reactor 40 are communicated with a gas treatment device 80, and the gas treatment device 80 comprises a gas condenser 81, a sulfuric acid solution absorber 82, a potassium iodide solution absorber 83, a sodium hydroxide absorber 84 and a vacuum pump 85 which are sequentially arranged along the gas discharge direction;
the reaction kettle wall of the first reactor 30 is provided with a first cooling water circulating device 91;
the second cooling water circulation device 92 is arranged on the reaction kettle wall of the second reactor 40.
Further, the first cooling water circulation device 91 includes a first cooling water circulation chamber 91a disposed from the outer wall of the middle portion of the first reactor 30 to the outer wall of the lower portion thereof, a first cooling liquid inlet (for cooling circulating water to enter) is disposed on the side wall of the first cooling water circulation chamber 91a, and a first cooling liquid outlet (for cooling circulating water to exit) is disposed at the bottom of the first cooling water circulation chamber 91 a.
Further, the second cooling water circulation device 92 includes a second cooling water circulation cavity 92a disposed from the outer wall of the middle portion of the second reactor 40 to the outer wall of the lower portion thereof, a second cooling liquid inlet (for cooling circulating water to enter) is disposed on the side wall of the second cooling water circulation cavity 92a, and a second cooling liquid outlet (for cooling circulating water to exit) is disposed at the bottom of the second cooling water circulation cavity 92 a.
Further, the output end of the citric acid inlet tank 12 is provided with a first pump a1, and the output end of the first pump a1 is connected with the upper part of the first reactor 30.
Still further, the bottom of the first reactor 30 is provided with a first reactant outlet, the output end of the first reactant outlet is provided with a second pump a2, and the output end of the second pump a2 is connected with the upper part of the second reactor 40.
Still further, the bottom of the second reactor 40 is provided with a second reactant outlet, an output end of the second reactant outlet is provided with a third pump a3, an output end of the third pump a3 is connected with the middle part of the plate-and-frame filter press 50, the upper part of the plate-and-frame filter press 50 is connected with the sewage treatment device 70, and the lower part of the plate-and-frame filter press 50 is connected with the incineration treatment device 60.
The technical scheme adopted by the utility model, namely the disposal method
The principle of the treatment method is as follows: the method comprises the steps of taking waste sodium chlorite (solid) as a main disposal object, firstly using pure water to dissolve and pretreat (the content of available chlorine: 105%), then pumping a citric acid solution into a reactor, reacting the sodium chlorite and the citric acid to form sodium citrate, chlorine dioxide, sodium chloride and water, and decomposing chlorine dioxide in a system to form hydrogen chloride, carbon dioxide and water by using a formaldehyde solution as a reaction medicament in a mixed solution. And simultaneously, under an acidic condition, potassium iodide solution is adopted to completely remove chlorine dioxide to form potassium iodide, potassium sulfate, iodine and water, and then sodium hydroxide is added to adjust the pH value to 8.0. And finally, carrying out plate-and-frame filter pressing on the solid-liquid mixed solution, recycling the filtrate after evaporation desalination and biochemical treatment, and carrying out incineration treatment on the filter residue in a rotary kiln.
The reaction mechanism is as follows:
NaClO2+C6H8O7→Na3C6H5O7+ClO2+NaCl+H2O
ClO2+HCHO+H2O→HCOOH+HCl
ClO2+HCOOH→HCl+CO2↑+H2O
ClO2+KI+HCl→KCl+I2+H2O
NaOH+HCl→NaCl+H2O
the disposal method comprises the following steps:
1) reacting sodium chlorite with citric acid: after scrap sodium chlorite is added into a first reactor 30, pure water is added for dissolution, and then citric acid solution is added through a first medicine adding device 10 for reaction, so that the sodium chlorite is decomposed into sodium citrate, chlorine dioxide, sodium chloride and water;
2) reacting chlorine dioxide with formaldehyde: pumping the mixed solution treated in the step 1) into a second reactor 40, adding a formaldehyde solution into the mixed solution through a second medicine adding device 20, and decomposing the chlorine dioxide through two steps of reaction to form carbon dioxide, hydrogen chloride and water; adding potassium iodide solution through a second medicine adding device 20, on one hand, verifying whether chlorine dioxide completely reacts, on the other hand, completely reacting excessive chlorine dioxide, adding sodium hydroxide solution into the solution after the reaction, and adjusting the pH value to about 8.0;
3) cooling: a large amount of heat energy is released in the reaction process of the step 1) and the step 2), and the temperature of a reaction system is controlled below 40 ℃ by cooling through circulating cooling water;
4) a solid-liquid separation system: carrying out plate-and-frame filter pressing on the mixed solution treated in the step 2), sending residues obtained after filter pressing to a rotary kiln for incineration treatment, and carrying out biochemical treatment on filter pressing wastewater after evaporation and desalination.
The embodiments of the present invention will be described in detail below with reference to the accompanying drawings.
Example 1: adding 10kg (+ -1%) of sodium chlorite into a first reactor 30, adding 90L (+ -1%) of sodium chlorite for dissolving, slowly adding 12L (+ -1%) of 50% of citric acid solution through a medicine adding pump, stirring for reacting for 5 hours, pumping the mixed solution into a second reactor 40 through a slurry pump, slowly adding 4.5L (+ -1%) of 30% of formaldehyde solution, stirring for reacting for 3 hours, adding 1L (+ -1%) of 10% of potassium iodide solution for reacting for 1 hour, then adding 6.5kg of sodium hydroxide for adjusting the pH value to 8.0, finally performing solid-liquid separation through plate and frame filter pressing, sending a filter cake to a rotary kiln for incineration disposal, and performing evaporation desalination on filter pressing wastewater for biochemical disposal. The reaction process is stable, and no abnormal condition occurs.
Detecting the filtrate, wherein the detection data are as follows: pH: 8.56, available chlorine content: 0.15%, no heavy metal was detected.
Example 2: adding 10kg (+ -1%) of sodium chlorite into a first reactor 30, adding 90L (+ -1%) of sodium chlorite for dissolving, slowly adding 14L (+ -1%) of 50% of citric acid solution through a medicine adding pump, stirring for reacting for 5 hours, pumping the mixed solution into a second reactor 40 through a slurry pump, slowly adding 5.5L (+ -1%) of 30% of formaldehyde solution, stirring for reacting for 3 hours, adding 1.6L (+ -1%) of 10% of potassium iodide solution for reacting for 1 hour, then adding 7kg of sodium hydroxide for adjusting the pH value to 8.0, finally performing solid-liquid separation through plate and frame filter pressing, sending a filter cake to a rotary kiln for incineration disposal, and performing evaporation desalination on filter pressing wastewater for biochemical disposal. The reaction process is stable, and no abnormal condition occurs.
Detecting the filtrate, wherein the detection data are as follows: pH: 8.78, available chlorine content: 0.2%, no heavy metal was detected.
Example 3: adding 10kg (+ -1%) of sodium chlorite into a first reactor 30, adding 90L (+ -1%) of sodium chlorite for dissolving, slowly adding 13.5L (+ -1%) of 50% citric acid solution through a medicine adding pump, stirring for reacting for 5 hours, pumping the mixed solution into a second reactor 40 through a slurry pump, slowly adding 4.9L (+ -1%) of 30% formaldehyde solution, stirring for reacting for 3 hours, adding 1.2L (+ -1%) of 10% potassium iodide solution for reacting for 1 hour, then adding 6.8kg of sodium hydroxide for adjusting the pH value to 8.0, finally performing solid-liquid separation through plate-and-frame filter pressing, sending a filter cake to a rotary kiln for incineration and filter pressing treatment, and performing biochemical treatment after evaporation and desalination on wastewater. The reaction process is stable, and no abnormal condition occurs.
Detecting the filtrate, wherein the detection data are as follows: pH: 8.66, available chlorine content: 0.1%, no heavy metal was detected.
Claims (8)
1. A safe processing device for scrapped sodium chlorite is characterized in that: comprises a first dosing device (10), a second dosing device (20), a first reactor (30), a second reactor (40), a plate frame filter press (50), an incineration disposal device (60) and a sewage treatment device (70);
the first medicine adding device (10) is arranged on the first reactor (30), and the first medicine adding device (10) comprises a sodium chlorite inlet tank (11), a citric acid inlet tank (12) and a pure water inlet tank (13); the lower part of the first reactor (30) is connected with the upper part of the second reactor (40), the second medicine adding device (20) is arranged on the second reactor (40), and the second medicine adding device (20) comprises a formaldehyde solution inlet groove (21), a potassium iodide solution inlet groove (22) and a sodium hydroxide solution inlet groove (23);
the lower part of the second reactor (40) is connected with a plate frame filter press (50), the upper part of the plate frame filter press (50) is connected with a sewage treatment device (70), and the lower part of the plate frame filter press (50) is connected with an incineration disposal device (60);
the upper parts of the first reactor (30) and the second reactor (40) are communicated with a gas treatment device (80);
a first cooling water circulating device (91) is arranged on the reaction kettle wall of the first reactor (30);
and a second cooling water circulating device (92) is arranged on the reaction kettle wall of the second reactor (40).
2. The device for safely disposing of discarded sodium chlorite according to claim 1, wherein: the upper part of the first reactor (30) is connected with a sodium chlorite inlet tank (11), a citric acid inlet tank (12) and a pure water inlet tank (13), the upper part of the second reactor (40) is provided with a formaldehyde solution inlet tank (21), a potassium iodide solution inlet tank (22) and a sodium hydroxide solution inlet tank (23), and the lower part of the second reactor (40) is connected with the middle part of the plate frame filter press (50).
3. The device for safely disposing of discarded sodium chlorite according to claim 1, wherein: the gas treatment device (80) comprises a gas condenser (81), a sulfuric acid solution absorber (82), a potassium iodide solution absorber (83), a sodium hydroxide absorber (84) and a vacuum pump (85) which are sequentially arranged along the gas discharge direction.
4. A device for safely disposing of discarded sodium chlorite according to claim 1, 2 or 3, wherein: the first cooling water circulation device (91) comprises a first cooling water circulation cavity (91a) arranged from the outer wall of the middle part of the first reactor (30) to the outer wall of the lower part of the first reactor, a first cooling liquid inlet is formed in the side wall of the first cooling water circulation cavity (91a), and a first cooling liquid outlet is formed in the bottom of the first cooling water circulation cavity (91 a).
5. A device for safely disposing of discarded sodium chlorite according to claim 1, 2 or 3, wherein: the second cooling water circulation device (92) comprises a second cooling water circulation cavity (92a) arranged from the outer wall of the middle part of the second reactor (40) to the outer wall of the lower part of the second reactor, a second cooling liquid inlet is arranged on the side wall of the second cooling water circulation cavity (92a), and a second cooling liquid outlet is arranged at the bottom of the second cooling water circulation cavity (92 a).
6. A device for safely disposing of discarded sodium chlorite according to claim 1, 2 or 3, wherein: the output end of the citric acid inlet tank (12) is provided with a first pump (a1), and the output end of the first pump (a1) is connected with the upper part of the first reactor (30); a first reactant outlet is arranged at the bottom of the first reactor (30), a second pump (a2) is arranged at the output end of the first reactant outlet, and the output end of the second pump (a2) is connected with the upper part of the second reactor (40); the bottom of the second reactor (40) is provided with a second reactant outlet, the output end of the second reactant outlet is provided with a third pump (a3), and the output end of the third pump (a3) is connected with the middle part of the plate frame filter press (50).
7. The device for safely disposing of discarded sodium chlorite according to claim 1, wherein: the first dosing device (10) is arranged in the first reactor (30), and a thermometer is also arranged in the first reactor (30); the second medicine adding device (20) is arranged in the second reactor (40), and a thermometer is further arranged in the second reactor (40).
8. A device for safely disposing of discarded sodium chlorite according to claim 1 or 3, which comprises: a buffer tank is provided in the gas processing device (80).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
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| CN202121451897.1U CN215609028U (en) | 2021-06-25 | 2021-06-25 | Safe processing device for scrapped sodium chlorite |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202121451897.1U CN215609028U (en) | 2021-06-25 | 2021-06-25 | Safe processing device for scrapped sodium chlorite |
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| CN215609028U true CN215609028U (en) | 2022-01-25 |
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| CN202121451897.1U Active CN215609028U (en) | 2021-06-25 | 2021-06-25 | Safe processing device for scrapped sodium chlorite |
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2021
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Address after: 230000 Wushan Town, Changfeng County, Hefei City, Anhui Province Patentee after: Anhui Haoyue Environmental Technology Co.,Ltd. Address before: 230000 Wushan Town, Changfeng County, Hefei City, Anhui Province Patentee before: ANHUI HAO YUE ENVIRONMENTAL TECHNOLOGY Co.,Ltd. |