CN216106466U - Phosphorus-containing wastewater treatment system - Google Patents
Phosphorus-containing wastewater treatment system Download PDFInfo
- Publication number
- CN216106466U CN216106466U CN202121206379.3U CN202121206379U CN216106466U CN 216106466 U CN216106466 U CN 216106466U CN 202121206379 U CN202121206379 U CN 202121206379U CN 216106466 U CN216106466 U CN 216106466U
- Authority
- CN
- China
- Prior art keywords
- tower
- phosphorus
- wastewater
- wet
- tank
- 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.)
- Active
Links
Images
Landscapes
- Removal Of Specific Substances (AREA)
- Treatment Of Water By Oxidation Or Reduction (AREA)
- Water Treatment By Electricity Or Magnetism (AREA)
Abstract
The utility model discloses a phosphorus-containing wastewater treatment system, which is used for realizing a comprehensive utilization method of phosphorus-containing wastewater, and mainly comprises an oxidation tank, a flocculation tank, an inclined tube sedimentation tank, a PH regulation tank, a reaction tank, a sedimentation tank, a concentration device and an electrolysis device in sequence according to the process flow, wherein the concentration device is followed by the electrolysis device, and comprises a wet tower, a dry tower, a wastewater preheater, an air preheater, a condensate water cooler, an air circulating fan, a strong brine circulating pump and a condensate water circulating pump.
Description
Technical Field
The utility model relates to a phosphorus-containing wastewater treatment system, in particular to a treatment system for acetylene gas cleaning wastewater in a calcium carbide-process PVC production process.
Background
In the industry of calcium carbide method polyvinyl chloride, most enterprises adopt a sodium hypochlorite solution to clean crude acetylene gas and remove PH contained in the acetylene gas3And H2S and the like. In industrial production, sodium hypochlorite with effective chlorine content (mass fraction, the same below) of 0.08% -0.12% is generally used for washing, and when the effective chlorine content is reduced to 0.06%, the sodium hypochlorite loses the capacity of removing gas impurities, and the part of the ineffective sodium hypochlorite is called waste sodium hypochlorite. The waste sodium hypochlorite has complex components and various parameters far higher than the emission index, so the waste sodium hypochlorite must be recovered in time. At present, the most widely applied mode in the industry is that after the waste sodium hypochlorite is blown away by compressed air to dissolve acetylene gas, about 70 percent of the waste sodium hypochlorite directly enters a generator to react with calcium carbide, and the rest of the waste sodium hypochlorite and high-concentration sodium hypochlorite or chlorine gas are prepared for recycling. Basically, the whole recycling of the waste sodium hypochlorite can be realized by the traditional mode, but with the further research and the production condition of the carbide slag cement, the recycling mode can hardly achieve the treatment effect and can not achieve the treatment effectOnly certain potential safety hazard is produced to sodium hypochlorite, and the production of downstream carbide slag cement and the quality of cement products are greatly influenced.
Chinese patent ZL201110041532.6 discloses a method for treating phosphorus-containing wastewater, which mainly comprises the steps of adding an oxidant into the phosphorus-containing wastewater to adjust the pH value, stirring and oxidizing the phosphorus-containing wastewater, adding a coagulant to adjust the pH value, and disclosing the related treatment method of the mixture of iron, aluminum and calcium and the mixing proportion of the coagulant. However, in the method, the wastewater after the fine treatment is discharged after being adsorbed and filtered, and the environmental protection and potential safety hazards still exist.
Chinese patent ZL201110420152.3 discloses a comprehensive treatment method for phosphorus-containing wastewater, which mainly comprises the steps of oxidation conversion, Fenton oxidation, coagulating sedimentation and the like, so that organic phosphorus, hypophosphite and other inorganic phosphorus in the wastewater are effectively removed. However, the patent method does not give better suggestions to the comprehensive treatment of subsequent water and a wastewater treatment system with higher requirements, and only can lead the wastewater to reach the discharge standard of the total phosphorus amount, so that the existing higher production process requirements and environmental protection standards cannot be met.
Disclosure of Invention
The utility model relates to a phosphorus-containing wastewater treatment system, in particular to a method for comprehensively utilizing acetylene gas cleaning wastewater in a calcium carbide-process PVC production process.
The utility model provides a disposal system for a comprehensive utilization method for treating phosphorus-containing wastewater, which comprises the following steps:
1) and phosphorus-containing wastewater is subjected to two-step phosphorus removal through oxidation by an oxidant and reprecipitation, and the total phosphorus content index is less than 5 mg/L.
2) Feeding the wastewater after phosphorus removal into a pH adjusting tank, feeding the wastewater with the pH stabilized at 7-8 into a reaction tank, adding activated carbon powder to remove COD and TOC in the water, wherein the COD and TOC indexes of the wastewater after fine treatment are less than 100mg/L, and the total phosphorus is less than 5 mg/L;
3) the refined wastewater enters a concentration device, and the salt content of the concentrated wastewater meets the inlet concentration of an electrolysis device, namely the NaCl content is 310 g/L;
4) and sending the concentrated wastewater into an electrolysis device, wherein the anolyte is: the concentration of the saturated NaCl solution is controlled,
the electrolysis product is chlorine and light salt water; the catholyte solution is: alkali liquor is added into the mixture,
the electrolysis product is hydrogen and 32% NaOH; the overall reaction formula is:
。
5) hydrogen is recycled to the production system, dilute brine flows back to the concentration device for recycling, chlorine and NaOH are compounded to form a sodium hypochlorite solution with the effective chlorine content (mass fraction) of 0.08-0.12% for recycling to the acetylene purification device, and the reaction equation is as follows:
。
the method for comprehensively utilizing the phosphorus-containing wastewater comprises the following steps of (1) feeding the wastewater from a workshop into an oxidation pond, adding a Fenton reagent hydrogen peroxide: ferrous sulfate =1: 3; then the wastewater enters a flocculation tank for sedimentation.
The method for comprehensively utilizing the phosphorus-containing wastewater comprises the following steps of (1) precipitating in a flocculation tank, wherein the coagulant aid comprises PAC and PAM; the wastewater is settled in the inclined tube settling tank to remove suspended matters.
The method for comprehensively utilizing the phosphorus-containing wastewater comprises the step 3, wherein the concentration device comprises but is not limited to a wastewater concentration device formed by adopting a multi-effect technology (MEE), a Thermal Vapor Recompression (TVR) and a Mechanical Vapor Recompression (MVR).
The method for comprehensively utilizing the phosphorus-containing wastewater comprises the step 3, wherein the electrolytic device is an ionic membrane electrolytic device.
The disposal system for realizing the comprehensive utilization method of the phosphorus-containing wastewater mainly comprises an oxidation tank, a flocculation tank, an inclined tube sedimentation tank, a PH regulation tank, a reaction tank, a sedimentation tank, a concentration device and an electrolysis device according to the sequence of the process flow, wherein the electrolysis device is arranged behind the concentration device, and the electrolysis device is an ion membrane electrolysis device; the concentrating device comprises a wet tower, a dry tower, a wastewater preheater, an air preheater, a condensate cooler, an air circulating fan, a strong brine circulating pump and a condensate circulating pump, wherein the inlet at the upper part of the wet tower is provided with the wastewater preheater, the outlet at the upper part of the wet tower is provided with the air circulating fan, the bottom of the wet tower is provided with the strong brine circulating pump, qualified concentrated wastewater flows to an electrolysis device, the wastewater preheater enters the wet tower, saturated steam is connected with the inlet at the lower part of the dry tower through the outlet of the air circulating fan, the air preheater and the condensate cooler are arranged at the top of the dry tower, the air preheater is connected with the inlet at the lower part of the wet tower, the lower part of the dry tower is connected with the condensate circulating pump, the condensate cooler is connected with the dry tower, condensate recycling and the condensate circulating pump are connected to a condensate recycling subsequent system, and the lower part of the dry tower is provided with a pipeline for returning to a production system.
The wet tower is a packed tower, and upward hot air can be introduced into the wet tower.
The utility model has the beneficial effects that: the utility model utilizes the conventional medicament to carry out dephosphorization treatment on the wastewater, completes the comprehensive utilization of the wastewater through the treatment of a plurality of devices of wastewater oxidation, precipitation, concentration, electrolysis and recycling, achieves the zero discharge of the wastewater, particularly aims at the zero discharge treatment of the phosphorus-containing wastewater in the acetylene gas cleaning production process in the calcium carbide method PVC production process, and realizes the purposes that hydrogen is recycled to a production system, light salt water flows back to a concentration device for recycling, and chlorine and NaOH are compounded to form sodium hypochlorite solution for recycling to the acetylene cleaning device.
Drawings
FIG. 1 is a process flow diagram of an embodiment of the present invention;
FIG. 2 is a schematic view of the apparatus and process for comprehensive utilization of phosphorus-containing wastewater in FIG. 1.
In fig. 2: 1 is a wet tower; 2 is a dry tower; 3-1 is a waste water preheater; 3-2 is an air preheater; 4 is a condensed water cooler; 5 is an air circulating fan; 6 is a strong brine circulating pump; and 7 is a condensed water circulating pump.
Detailed Description
In order to explain the technical content, the objects and the effects of the present invention in detail, the following description will be given with reference to the embodiments.
Referring to the attached drawings 1-2, in order to achieve the above purpose, embodiment 1 of the utility model provides a comprehensive utilization method of phosphorus-containing wastewater, which is implemented by taking acetylene gas cleaning wastewater in a calcium carbide method PVC production process as an example, and aims to overcome the defects of the prior art and realize a process method for treating and subsequently producing and recycling the phosphorus-containing wastewater, and the method comprises the following steps:
phosphorus-containing wastewater is subjected to phosphorus removal through an oxidation and precipitation two-step method: the phosphorus-containing wastewater is sent into an oxidation pond, and a Fenton reagent hydrogen peroxide is added: ferrous sulfate =1: 3; then the mixture enters a flocculation tank for sedimentation, and the added coagulant aids comprise PAC and PAM; settling the wastewater in an inclined tube settling tank to remove suspended matters; adding sodium hydroxide to a pH adjusting tank to adjust the pH; adding active carbon in the reaction to adsorb COD and TOC; then, COD and TOC indexes of the sediment are less than 100mg/L, and the total phosphorus content index is less than 5 mg/L. The wastewater after dephosphorization is sent into a pH adjusting tank, the pH is controlled to be 7-8, then the wastewater is sent into a reaction tank, activated carbon powder is added to remove COD and TOC in the water, and the indexes of the COD and the TOC of the wastewater after fine treatment are less than 100 mg/L; the wastewater after the fine treatment enters a concentration device, and the salt content NaCl of the concentrated wastewater is 310 g/L; feeding the concentrated wastewater into an electrolysis device, wherein electrolysis products are hydrogen, sodium hydroxide, chlorine and light brine; the hydrogen is recycled to the production system, the dilute brine is refluxed to the concentration device for recycling, and the chlorine and the sodium hydroxide are compounded to form a sodium hypochlorite solution with the effective chlorine content (mass fraction) of 0.08-0.12% for recycling to the acetylene purification device. And (5) recycling the hydrogen to the HCl synthesizer, and continuously concentrating the light saline water.
The disposal system for realizing the comprehensive utilization method of the phosphorus-containing wastewater mainly comprises an oxidation tank, a flocculation tank, an inclined tube sedimentation tank, a PH regulation tank, a reaction tank, a sedimentation tank, a concentration device and an electrolysis device according to the sequence of the process flow, wherein the electrolysis device is arranged behind the concentration device, and the electrolysis device is an ion membrane electrolysis device; the concentration device comprises a wet tower 1, a dry tower 2, a wastewater preheater 3-1, an air preheater 3-2, a condensed water cooler 4, an air circulating fan 5, a strong brine circulating pump 6 and a condensed water circulating pump 7, wherein the wastewater preheater 3-1 is arranged at an inlet at the upper part of the wet tower 1, the air circulating fan 5 is arranged at an outlet at the upper part of the wet tower 1, the strong brine circulating pump 6 is arranged at the bottom of the wet tower 1, qualified concentrated wastewater is delivered to an electrolysis device, the wastewater preheater 3-1 enters the wet tower 1, saturated steam is connected with an inlet at the lower part of the dry tower 2 through an outlet of the air circulating fan 5, the air preheater 3-2 and the condensed water cooler 4 are arranged at the top of the dry tower 2, the air preheater 3-2 is connected with an inlet at the lower part of the wet tower 1, the lower part of the dry tower 2 is connected with the condensed water circulating pump 7, and the condensed water cooler 4 is connected with the dry tower 2, the condensed water recycling and the condensed water circulating pump 7 are connected to a condensed water recycling subsequent system, and the lower part of the drying tower 2 is provided with a pipeline which is recycled to the production system.
The wet tower is a packed tower, and upward hot air can be introduced into the wet tower.
After the effluent of the sedimentation tank is qualified (TOC and COD are less than 100 mg/L; total phosphorus is less than 5 mg/L), pumping the wastewater out by a pump, enabling the wastewater to enter the upper part of a wet tower 1 through a wastewater preheater 3-1 and spraying the wastewater into the wet tower (1), enabling the wet tower to be a packed tower, enabling the wastewater flowing out of the wet tower 1 to meet hot air upwards along the inside of the wet tower 1 through a packing layer for mass and heat transfer, enabling the hot air to take away redundant water in the wastewater to form saturated steam, pumping the saturated steam from an outlet at the upper part of the wet tower by an air circulating fan 5, enabling the falling concentrated wastewater to fall into the bottom of the wet tower, pumping the falling concentrated wastewater out by a strong brine circulating pump 6, feeding the concentrated wastewater with qualified salt content (NaCl is more than 310 g/L) into an electrolysis device, and enabling the unqualified concentrated wastewater and raw water (the wastewater which is not concentrated) to enter the wet tower through the wastewater preheater; saturated steam enters the dry tower from an inlet at the lower part of the dry tower 2 through an outlet of the air circulating fan, meets the falling cooler condensed water at the packing part of the dry tower for mass and heat transfer, the temperature is reduced to reduce the water content in the saturated air, the air with the excessive water removed flows out from the top of the dry tower, and the air is heated by an air preheater 3-2 and then enters the wet tower from an inlet at the lower part of the wet tower; the cooler condensed water falls into the lower part of the drying tower 2, is pumped out by a condensed water circulating pump 7, is cooled by a condensed water cooler 4, and is sprayed into the drying tower from an inlet at the upper part of the drying tower, and in order to keep the liquid level at the lower part of the drying tower 2 within a certain safety range, the redundant condensed water is recycled to a production system.
While the foregoing is directed to the preferred embodiment of the present invention, it will be understood that it is not intended to be exhaustive or to limit the utility model to the precise form disclosed, and that various modifications and adaptations may be resorted to without departing from the principles of the utility model and are intended to those skilled in the art by virtue of the fact that the utility model is described in detail and with the understanding that various embodiments of the utility model are suited to the particular use contemplated.
Claims (3)
1. A phosphorus-containing wastewater treatment system is characterized in that: the system mainly comprises an oxidation pond, a flocculation tank, an inclined tube sedimentation tank, a PH adjusting tank, a reaction tank, a sedimentation tank, a concentration device and an electrolysis device according to the sequence of the process flow, wherein the concentration device comprises a wet tower, a dry tower, a wastewater preheater, an air preheater, a condensed water cooler, an air circulating fan, a strong brine circulating pump and a condensed water circulating pump.
2. The phosphorus-containing wastewater treatment system according to claim 1, wherein: the inlet of wet tower upper portion is provided with waste water preheater, wet tower upper portion export is provided with air circulating fan, wet tower bottom is provided with the strong brine circulating pump, qualified concentrated waste water to electrolytic device, waste water preheater gets into wet tower, saturated steam links to each other by dry tower lower part entry through the air circulating fan export, there are air preheater and condensate cooler at dry tower top of the tower, air preheater links to each other with wet tower lower part import, the dry tower lower part links to each other with the condensate circulating pump, the condensate cooler links to each other with the dry tower, the condensate water retrieval and utilization links to condensate water retrieval and utilization subsequence system with the condensate circulating pump mutually, and there is the pipeline of returning to production system dry tower lower part.
3. The phosphorus-containing wastewater treatment system according to claim 2, wherein: the wet tower is a packed tower, and upward hot air can be introduced into the wet tower.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202121206379.3U CN216106466U (en) | 2021-06-01 | 2021-06-01 | Phosphorus-containing wastewater treatment system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202121206379.3U CN216106466U (en) | 2021-06-01 | 2021-06-01 | Phosphorus-containing wastewater treatment system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN216106466U true CN216106466U (en) | 2022-03-22 |
Family
ID=80719978
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202121206379.3U Active CN216106466U (en) | 2021-06-01 | 2021-06-01 | Phosphorus-containing wastewater treatment system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN216106466U (en) |
-
2021
- 2021-06-01 CN CN202121206379.3U patent/CN216106466U/en active Active
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN106495404B (en) | A kind of processing method of the high salinity cupric organic wastewater of highly acidity | |
| CN105439358A (en) | Method and device for realizing zero discharge of desulfurization wastewater | |
| CN107585968B (en) | A kind of chlor-alkali brine waste processing system and method | |
| CN106746016A (en) | A kind of method and apparatus for processing waste water | |
| CN104402156B (en) | Special-purpose equipment for coal chemical high brine purification, evaporative crystallization and recovery technology | |
| CN113880340B (en) | Method for purifying byproduct sodium chloride in organic silicon high-salt wastewater | |
| CN110835199A (en) | Electroplating wastewater zero-discharge treatment system and treatment process thereof | |
| CN103553246A (en) | Device and method for softening hard water by using carbon dioxide in flue gas | |
| CN104909494A (en) | Process for impurity removal and purification of industrial high-concentration brine and special equipment of process | |
| CN104817157A (en) | Chemical wastewater pretreatment method and sequencing-batch alkaline hydrolysis reactor | |
| CN113698002A (en) | Novel reverse osmosis strong brine recovery treatment process | |
| CN216106466U (en) | Phosphorus-containing wastewater treatment system | |
| CN216073436U (en) | Comprehensive utilization device for phosphorus-containing wastewater | |
| CN108249670A (en) | A kind of acid etching liquid treatment acid solution and the technique for recycling copper | |
| CN105000745B (en) | A kind of sulfur Gas Fields produced water treatment system | |
| CN115432874A (en) | Comprehensive utilization method of phosphorus-containing wastewater | |
| CN206580692U (en) | A kind of photovoltaic industry fluoride waste recycling and the system of reuse | |
| CN113816526B (en) | Water quenching water recycling treatment process for cold rolling continuous annealing unit | |
| CN101456638A (en) | Light salt brine purification and reuse technology in industrial process | |
| CN112194298B (en) | System and method for recycling wastewater of whole power plant | |
| CN107540139B (en) | Recycling treatment system and method for cold rolling wastewater ion exchange strong brine | |
| US2000197A (en) | Method of treating water | |
| CN114956433A (en) | Three-waste cooperative treatment process system in granular silicon production process | |
| CN204237642U (en) | A kind of special purpose device of Coal Chemical Industry haline water purification process technique | |
| CN210214990U (en) | Zero discharge system for cyclic and comprehensive utilization of waste water of chlor-alkali enterprise |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant |