CN212403781U - But resource recovery's desulfurization effluent disposal system - Google Patents
But resource recovery's desulfurization effluent disposal system Download PDFInfo
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- CN212403781U CN212403781U CN202020349690.2U CN202020349690U CN212403781U CN 212403781 U CN212403781 U CN 212403781U CN 202020349690 U CN202020349690 U CN 202020349690U CN 212403781 U CN212403781 U CN 212403781U
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Abstract
The utility model relates to the technical field of environmental protection, in particular to a desulfurization wastewater treatment system capable of recycling resources, which comprises a three-header mechanism, a chemical softening mechanism, a nanofiltration mechanism, a reverse osmosis mechanism, a resin adsorption mechanism, a bipolar membrane electrodialysis mechanism and a neutralization tank; the triple box mechanism, the chemical softening mechanism, the nanofiltration mechanism, the reverse osmosis mechanism, the resin adsorption mechanism and the bipolar membrane electrodialysis mechanism are sequentially communicated; the bipolar membrane electrodialysis mechanism is communicated with the reverse osmosis mechanism in a reverse direction, and the neutralization tank is arranged on a passage communicated in the reverse direction. The utility model discloses can effectively avoid mixing salt production and prepare out hydrochloric acid and sodium hydroxide solution, the many kinds of technologies of the acid-base retrieval and utilization power plant of production realize desulfurization waste water's zero release and resourceization, and the settlement of three header mechanisms, chemical softening mechanism and resin adsorption mechanism has also improved the life of membrane module to a certain extent, has reduced the problem of membrane pollution.
Description
Technical Field
The utility model belongs to the technical field of the environmental protection technique and specifically relates to a but resource recovery's desulfurization effluent disposal system is related to.
Background
In recent years, a great deal of research results have been obtained in the desulfurization technology of thermal power plants at home and abroad. Among them, the limestone-gypsum wet flue gas desulfurization technique is the most important technique for desulfurization, and has the advantages of mature technique, wide application range, high desulfurization efficiency, rich desulfurizer resources, reliable system operation, excellent variable load operation characteristics and the like, and the technique is widely applied to thermal power plants in China. However, in the wet desulfurization process, the generated desulfurization wastewater becomes industrial wastewater which is difficult to treat at the tail end of a power plant due to the characteristics of many accompanying suspended matters, high salt content, rich heavy metals, complex components and the like.
The traditional desulfurization wastewater treatment method, namely a triple box method, has mature technology and low process flow and investment operation cost, but cannot meet the requirement of zero wastewater discharge, and effluent of the methodStill contains a large amount of dissolved salts, and the direct discharge causes great harm to the environment. At present, available zero-emission technologies such as flue spray drying, pretreatment-evaporative crystallization, membrane treatment technologies and the like can realize zero-emission treatment of desulfurization wastewater. However, the flue spray drying method has the defects of easy generation of accumulated dust blockage, equipment corrosion, large amount of chlorine entering the fly ash and the like; the crystal salt evaporated by the pretreatment-evaporative crystallization method is mostly NaCl and NaSO4Some miscellaneous salts composed of the same components are even classified as hazardous waste, the disposal cost is high, and the crystallized salt generated at the tail end is difficult to be commercially circulated due to low purity; the key technical problem of membrane treatment application is the problems of membrane pollution and membrane service life, and the components of the wastewater are complex, so that the membrane treatment application has great influence on the service efficiency and the service life of the membrane.
At present, the deep treatment of the desulfurization wastewater can be realized by adopting the combination of different types of membrane technologies, and higher reuse water yield can be obtained, but the investment and operation cost is high, and the problems of membrane pollution and membrane service life are not solved.
SUMMERY OF THE UTILITY MODEL
The first purpose of the utility model is to provide a resource-recoverable desulfurization wastewater treatment system, which has low investment and operation cost, can realize resource recovery and utilization, and solves the problems of membrane pollution and membrane service life existing in the prior membrane treatment technology;
the utility model provides a desulfurization wastewater treatment system capable of recycling resources, which comprises a three-header mechanism, a chemical softening mechanism, a nanofiltration mechanism, a reverse osmosis mechanism, a resin adsorption mechanism, a bipolar membrane electrodialysis mechanism and a neutralization tank;
the triple box mechanism, the chemical softening mechanism, the nanofiltration mechanism, the reverse osmosis mechanism, the resin adsorption mechanism and the bipolar membrane electrodialysis mechanism are sequentially communicated;
the bipolar membrane electrodialysis mechanism is communicated with the reverse osmosis mechanism in a reverse direction, and the neutralization tank is arranged on a passage communicated in the reverse direction.
The utility model discloses an among the desulfurization effluent disposal system, three header mechanisms, chemical softening mechanism, receive and strain mechanism, reverse osmosis mechanism, resin adsorption mechanism, bipolar membrane electrodialysis mechanism and communicate in proper order, and bipolar membrane electrodialysis mechanism and reverse osmosis mechanism are reverse to be communicated, and the neutralization pond setting is on the passageway of reverse intercommunication. Part of heavy metals and suspended matters in the desulfurization wastewater generated by wet desulfurization in a thermal power plant are removed by a triple box mechanism, clarified effluent enters a chemical softening mechanism to reduce the concentration of calcium and magnesium ions in the wastewater, the wastewater treated by the triple box mechanism and the chemical softening mechanism is treated by a nanofiltration mechanism, the service life of a membrane can be prolonged, membrane pollution is reduced, divalent salts in a water body can be removed in the nanofiltration mechanism, generated monovalent salts enter a reverse osmosis mechanism to be concentrated and reduced to obtain reverse osmosis fresh water and concentrated brine, the reverse osmosis fresh water can be stored in a container for other processes, concentrated brine generated by reverse osmosis is pumped into a resin adsorption mechanism to further remove impurities, so that excessive impurities are prevented from entering a bipolar membrane electrodialysis mechanism, the service life of a novel ion exchange membrane is reduced, and water can be dissociated into hydrogen ions and hydroxyl ions under the action of a direct current electric field in the bipolar membrane electrodialysis mechanism, hydrochloric acid and sodium hydroxide are prepared, and zero emission and resource utilization of the desulfurization wastewater are realized. The bipolar membrane electrodialysis mechanism is reversely communicated with the reverse osmosis mechanism, the neutralization tank is arranged on a passage where the reverse communication is located, and the residual weak brine treated by the bipolar membrane electrodialysis mechanism is pumped into the reverse osmosis mechanism for recycling after the pH value of the residual weak brine is adjusted to a proper range by the neutralization tank. The utility model discloses can effectively avoid mixing salt production and prepare out hydrochloric acid and sodium hydroxide solution, the many kinds of technologies of the acid-base retrieval and utilization power plant of production realize desulfurization waste water's zero release and resourceization, reduce the running cost, and the setting for of three header mechanisms, chemical softening mechanism and resin adsorption mechanism has also improved the life of membrane module to a certain extent, has reduced the problem of membrane pollution.
Furthermore, a regulating tank is arranged between the reverse osmosis mechanism and the resin adsorption mechanism or between the resin adsorption mechanism and the bipolar membrane electrodialysis mechanism.
The regulating reservoir is arranged between the reverse osmosis mechanism and the resin adsorption mechanism or between the resin adsorption mechanism and the bipolar membrane electroosmosis mechanism. The adjusting tank is mainly used for adjusting the wastewater entering the bipolar membrane electrodialysis mechanism to enable the wastewater to have proper conductivity and pH value, and further the dissociation rate of the bipolar membrane electrodialysis mechanism to the wastewater is improved.
Further, a stirrer, a conductivity meter, a turbidity meter and a pH on-line monitor are arranged in the regulating reservoir.
Be provided with agitator, conductivity meter, turbidity appearance and pH on-line monitoring appearance in the equalizing basin, the agitator can carry out abundant mixing to the waste water in the equalizing basin, and the liquid level in the equalizing basin is all not crossed to conductivity meter and turbidity appearance and pH on-line monitoring appearance's probe for detect the mass concentration of well sodium chloride of waste water, the muddy degree and the pH of waste water in real time.
Furthermore, the nanofiltration mechanism comprises a plurality of stages of nanofiltration membrane assemblies which are connected in series in sequence, and the reverse osmosis mechanism comprises a plurality of stages of reverse osmosis membrane assemblies which are connected in series in sequence;
the chemical softening mechanism is communicated with the first-stage nanofiltration membrane component, the last-stage nanofiltration membrane component is communicated with the first reverse osmosis membrane component, and the last-stage reverse osmosis membrane component is communicated with the regulating tank or the resin adsorption mechanism.
The nanofiltration mechanism comprises a plurality of stages of reverse osmosis membrane components which are sequentially connected in series, the reverse osmosis mechanism comprises a plurality of stages of reverse osmosis membrane components which are sequentially connected in series, the chemical softening mechanism is communicated with the first stage of reverse osmosis membrane component, the last stage of nanofiltration membrane component is communicated with the first reverse osmosis membrane component, and the last stage of reverse osmosis membrane component is communicated with the regulating tank or the resin adsorption mechanism. By the arrangement, the long-term stable operation of the membrane component can be realized while the concentration processing multiple and the water outlet speed are ensured, the membrane pollution problem is effectively controlled, and the membrane service life is reduced due to frequent regeneration of the membrane.
The utility model also discloses a method of above-mentioned processing system treatment waste water, including following step:
s1, pretreating the desulfurization wastewater by using the triple box mechanism to obtain a supernatant;
s2, discharging the supernatant to the chemical softening mechanism, and adding alkali to reduce the concentration of calcium and magnesium ions;
s3, discharging the wastewater treated by the chemical softening mechanism into the nanofiltration mechanism to respectively obtain wastewater containing divalent salt and wastewater containing monovalent salt;
s4, discharging the wastewater containing monovalent salt to the reverse osmosis mechanism to respectively obtain fresh water and strong brine;
s5, discharging the strong brine to the resin adsorption mechanism to remove impurities in the wastewater;
s6, discharging the wastewater treated by the resin adsorption mechanism into the bipolar membrane electrodialysis mechanism to respectively obtain acid liquor and alkali liquor.
The method for treating the wastewater by using the desulfurization wastewater treatment system comprises the following steps: pumping the desulfurization wastewater into a triple box mechanism to remove part of hardness, heavy metal ions, suspended matters and the like; clear effluent of the triple box overflows into a chemical softening mechanism, and calcium and magnesium ions are removed by adding a medicament, so that the hardness of the wastewater is reduced; the effluent of the chemical softening mechanism is connected to a nanofiltration mechanism for salt separation treatment, the generated monovalent salt wastewater enters a next-stage reverse osmosis mechanism, and the divalent salt wastewater is pumped into a triple box mechanism to realize resource recycling; the monovalent salt wastewater separated by the nanofiltration mechanism enters a reverse osmosis mechanism for concentration and reduction treatment to obtain fresh water and concentrated salt water; pumping the concentrated saline water into a resin adsorption mechanism to remove impurities in the water body; and discharging the wastewater treated by the resin adsorption mechanism into a bipolar membrane electrodialysis mechanism, dissociating water into hydrogen ions and hydroxyl ions, preparing hydrochloric acid and sodium hydroxide, and realizing zero emission and recycling of the desulfurization wastewater.
Further, step S2 specifically includes: discharging the supernatant to the chemical softening mechanism, adding NaOH or Ca (OH)2Any one or two of the above-mentioned two substances, and controlling pH value to be not less than 11 so as to reduce magnesium ion concentration in the waste water; adding Na again2CO3Keeping the reaction for 30-50min, and reducing the concentration of calcium ions in the wastewater; and finally, adding a flocculating agent with the mass concentration of 0.1-0.3%, and adjusting the hardness of the effluent to be less than 80ppm and the turbidity to be less than 1.0 NTU.
Discharging the supernatant treated by the triple box mechanism into a chemical softening mechanism, adding NaOH or Ca (OH)2Either or both of them, and controlling the pH value to be not less than 11 to make the magnesium ions in the waste water be Mg (OH)2Form precipitation is carried out, the concentration of magnesium ions in the wastewater is reduced, and alkali liquor obtained by a subsequent bipolar membrane electrodialysis mechanism can also be used; adding Na again2CO3Keeping the reaction for 30-50min to make the calcium ions in the wastewater Ca (OH)2Form precipitation is carried out, and the concentration of calcium ions in the wastewater is reduced; and finally, adding a flocculating agent PAM with the mass concentration of 0.1-0.3%, and adjusting the hardness of the effluent to be less than 80ppm and the turbidity to be less than 1.0 NTU.
Further, in step S3, when the nanofiltration mechanism is operated, the operation pressure is controlled to be less than 2.5MPa, the turbidity is controlled to be less than 1.0NTU, and the pH of the inlet water is controlled to be 4-9.
When the nanofiltration mechanism operates, the operating pressure is controlled to be less than 2.5MPa, the turbidity is controlled to be less than 1.0NTU, the pH of inlet water is 4-9, the outlet water speed can be effectively improved, and the service life of the membrane can be effectively prolonged.
Further, in step S4, when the reverse osmosis mechanism operates, the operation pressure is controlled to be 0.1-0.3MPa, and the water inlet flow is controlled to be 4-20m3H, turbidity less than 1.0 NTU.
When the reverse osmosis mechanism operates, the operation pressure is controlled to be 0.1-0.3MPa, and the water inlet flow is controlled to be 4-20m3The turbidity is less than 1.0NTU, the concentration multiple of the wastewater can be effectively improved, and the long-term stable operation of the membrane treatment unit is realized.
Further, step S5 specifically includes: discharging the concentrated brine to the regulating tank, and regulating the mass concentration of sodium chloride in the concentrated brine to be 6-8%, the pH value to be 7-9 and the conductivity to be 80-100 ms/cm; and discharging the effluent of the regulating reservoir to the resin adsorption mechanism, controlling the flow rate to be 5-10m/h, controlling the pH to be 7-9, controlling the resin expansion rate to be less than 35%, and controlling the hardness of the wastewater treated by the resin adsorption mechanism to be less than 4 ppm.
The mass concentration of sodium chloride in the concentrated salt water is adjusted to be 6-8%, the pH value is 7-9, the conductivity is 80-100ms/cm through the adjusting tank, and the dissociation rate of the bipolar membrane electrodialysis on the wastewater can be effectively improved; the wastewater which is adjusted to be qualified by the adjusting tank is discharged into the resin adsorption mechanism, impurities in the water body are further removed, the flow rate is controlled to be 5-10m/h, the pH value is controlled to be 7-9 because the filler in the resin adsorption mechanism is macroporous adsorption chelate resin, the resin adsorption rate can be provided, the resin expansion rate is ensured to be less than 35% in the resin adsorption process, the long-term stable operation of the resin adsorption mechanism can be realized, and the service life of the resin adsorption mechanism is prolonged.
Further, step S6 specifically includes: discharging the wastewater treated by the resin adsorption mechanism into the bipolar membrane electrodialysis mechanism, pumping the residual weak brine treated by the bipolar membrane electrodialysis mechanism into the neutralization tank to adjust the pH value to 7-8, and pumping the weak brine into the reverse osmosis mechanism for continuous treatment;
when the bipolar membrane electrodialysis mechanism runs, the volume of initial liquid of a salt chamber, an acid chamber and an alkali chamber of the bipolar membrane electrodialysis mechanism is 1:1:1, the volume of electrode liquid is 2-4% NaOH, the circulation flow of the salt liquid is 6-10t/h, the circulation flow of the obtained acid liquid is 6-10t/h, and the circulation flow of the obtained alkali liquid is 6-10 t/h.
The bipolar membrane electrodialysis operation mode is that water is circularly fed, namely acid, alkali and salt chamber inlet and outlet water are respectively arranged in the same container, the salt concentration of the initial inlet water is more than or equal to 6%, the initial solution of the acid and alkali chamber is fresh water generated in the reverse osmosis mechanism, the electrode solution is 2-4% NaOH, the circulation flow of the salt solution is 6-10t/h, the circulation flow of the obtained acid solution is 6-10t/h, and the circulation flow of the obtained alkali solution is 6-10 t/h. The method can obtain acid-alkali liquor in a shorter treatment period, the obtained acid-alkali liquor is respectively stored in the acid liquor storage tank and the alkali liquor storage tank, the obtained acid-alkali liquor can be reused by other equipment, and the resource recycling of the wastewater is improved.
The utility model discloses a desulfurization effluent disposal system compares with prior art, has following advantage:
the utility model discloses an among the desulfurization effluent disposal system, receive with three header mechanisms, chemical softening mechanism and resin adsorption mechanism and membrane treatment technique and strain, reverse osmosis, bipolar membrane electrodialysis combination use, the whole operation maintenance cost of system is low, and each treatment mechanism both plays the effect separately and promotes each other, has realized desulfurization waste water's zero release and resourceization. The chemical softening mechanism can effectively remove calcium and magnesium ions in the desulfurization wastewater, and effectively avoids the problems of blockage and pollution of subsequent membrane process equipment; the nanofiltration and reverse osmosis mechanism can effectively reduce the desulfurization wastewater, and the nanofiltration mechanism can separate the salt of the mixed salt in the desulfurization wastewater, so that the utilization rate of the inorganic salt component in the desulfurization wastewater is improved; the resin adsorption mechanism can further reduce the hardness of the wastewater and deeply remove impurities in the brine, and the acid and alkali quality of the bipolar membrane electrodialysis mechanism is improved. In addition, the arrangement of the neutralization pond can effectively buffer the increase of hydrogen ion concentration caused by ion reverse migration in the bipolar membrane electrodialysis process, so that the problem of low bipolar membrane electrodialysis efficiency is caused. The utility model discloses can effectively avoid mixing salt production and prepare out hydrochloric acid and sodium hydroxide solution, obtain acid-base liquid in the shorter period, the multiple technology of the acid-base retrieval and utilization power plant of production realizes desulfurization waste water's zero release and resourceization, and the settlement of three header mechanisms, chemical softening mechanism and resin adsorption mechanism has also improved the life of membrane module to a certain extent, has reduced the problem of membrane pollution.
Drawings
In order to more clearly illustrate the embodiments of the present invention or the technical solutions in the prior art, the drawings used in the embodiments or the technical solutions in the prior art will be briefly described below, and it is obvious that the drawings in the following description are some embodiments of the present invention, and for those skilled in the art, other drawings can be obtained according to these drawings without creative efforts.
FIG. 1 is a schematic view of a desulfurization wastewater treatment system of the present invention;
FIG. 2 is a process flow diagram of the desulfurization wastewater treatment method of the present invention.
Description of reference numerals:
1: a triple box mechanism; 2: a chemical softening mechanism; 3: a nanofiltration mechanism; 4: a reverse osmosis mechanism; 5: a resin adsorption mechanism; 6: a bipolar membrane electrodialysis mechanism; 7: a neutralization pond; 8: a regulating tank; 9: an acid liquor storage tank; 10: an alkali liquor storage tank.
Detailed Description
The technical solution of the present invention will be described clearly and completely with reference to the following embodiments, and it should be understood that the described embodiments are some, but not all embodiments of the present invention. Based on the embodiments in the present invention, all other embodiments obtained by a person skilled in the art without creative work belong to the protection scope of the present invention.
In the description of the present invention, it is to be understood that the terms "center", "longitudinal", "lateral", "length", "width", "thickness", "upper", "lower", "front", "rear", "left", "right", "vertical", "horizontal", "top", "bottom", "inner", "outer", "clockwise", "counterclockwise" and the like indicate orientations or positional relationships based on the orientations or positional relationships shown in the drawings, and are only for convenience of description and to simplify the description, but do not indicate or imply that the device or element referred to must have a particular orientation, be constructed and operated in a particular orientation, and therefore should not be construed as limiting the present invention.
Furthermore, the terms "first", "second" and "first" are used for descriptive purposes only and are not to be construed as indicating or implying relative importance or implicitly indicating the number of technical features indicated. Thus, features defined as "first", "second", may explicitly or implicitly include one or more of the described features. In the description of the present invention, "a plurality" means two or more unless specifically limited otherwise. Furthermore, the terms "mounted," "connected," and "connected" are to be construed broadly and may, for example, be fixedly connected, detachably connected, or integrally connected; can be mechanically or electrically connected; they may be connected directly or indirectly through intervening media, or they may be interconnected between two elements. The specific meaning of the above terms in the present invention can be understood in specific cases to those skilled in the art.
As shown in fig. 1, the desulfurization wastewater treatment system of the present invention comprises a triple box mechanism 1, a chemical softening mechanism 2, a nanofiltration mechanism 3, a reverse osmosis mechanism 4, a resin adsorption mechanism 5, a bipolar membrane electrodialysis mechanism 6 and a neutralization tank 7; the triple box mechanism 1, the chemical softening mechanism 2, the nanofiltration mechanism 3, the reverse osmosis mechanism 4, the resin adsorption mechanism 5 and the bipolar membrane electrodialysis mechanism 6 are communicated in sequence; the bipolar membrane electrodialysis mechanism 6 is reversely communicated with the reverse osmosis mechanism 4, and the neutralization pond 7 is arranged on a reversely communicated passage.
In the desulfurization wastewater treatment system of the utility model, the triple box mechanism 1, the chemical softening mechanism 2, the nanofiltration mechanism 3, the reverse osmosis mechanism 4, the resin adsorption mechanism 5 and the bipolar membrane electrodialysis mechanism 6, the triple box mechanism 1 can preliminarily reduce heavy metal ions and suspended matters in wastewater, the chemical softening mechanism 2 can effectively remove calcium and magnesium ions in the desulfurization wastewater, and the problems of blockage and pollution of subsequent membrane process equipment are effectively avoided; the nanofiltration and reverse osmosis mechanism 4 can effectively reduce the desulfurization wastewater, and the nanofiltration mechanism 3 can separate the mixed salt in the desulfurization wastewater, so that the utilization rate of the inorganic salt component in the desulfurization wastewater is improved; the resin adsorption mechanism 5 can further reduce the hardness of wastewater and deeply remove impurities in brine, so that the acid and alkali quality of the bipolar membrane electrodialysis mechanism 6 is improved, the service life of the membrane can be prolonged, membrane pollution is reduced, and the long-term stable operation of the treatment system is realized. In addition, the neutralization tank 7 is arranged on a reversely communicated passage, which can effectively buffer the increase of hydrogen ion concentration caused by the reverse migration of ions in the bipolar membrane electrodialysis process, and causes the problem of low efficiency of the bipolar membrane electrodialysis.
On the basis of the technical scheme, a regulating tank 8 is further arranged between the reverse osmosis mechanism 4 and the resin adsorption mechanism 5 or between the resin adsorption mechanism 5 and the bipolar membrane electrodialysis mechanism 6.
When the bipolar membrane electrodialysis mechanism 6 operates, the mass concentration, the pH value, the turbidity value and the conductivity value of sodium chloride in inlet water can influence the acid-base efficiency of electrodialysis, so that an adjusting tank 8 needs to be arranged between the reverse osmosis mechanism 4 and the bipolar membrane electrodialysis mechanism 6, and the adjusting tank 8 can be arranged between the reverse osmosis mechanism 4 and the resin adsorption mechanism 5 or between the resin adsorption mechanism 5 and the bipolar membrane electrodialysis mechanism 6.
In order to facilitate the detection of the regulating tank 8 on the conductivity, the pH value and the turbidity of the wastewater, a stirrer, a conductivity meter, a turbidity meter and an online pH monitor are arranged in the regulating tank 8.
Be provided with the agitator in the equalizing basin 8, the agitator set up the position in order to guarantee that the stirring rake completely submerges waste water can, and conductivity meter, turbidity appearance and pH on-line monitoring appearance's controller arranges the outside of equalizing basin 8 in, and the inside of equalizing basin 8 is arranged in to its probe to submerge the surface of water as the standard.
On the basis of the above technical scheme, preferably, the nanofiltration mechanism 3 comprises a plurality of stages of nanofiltration membrane modules connected in series in sequence, and the reverse osmosis mechanism 4 comprises a plurality of stages of reverse osmosis membrane modules connected in series in sequence; the chemical softening mechanism 2 is communicated with the first stage of the nanofiltration membrane component, the last stage of the nanofiltration membrane component is communicated with the first reverse osmosis membrane component, and the last stage of the reverse osmosis membrane component is communicated with the regulating tank 8 or the resin adsorption mechanism 5.
The nanofiltration mechanism 3 comprises a plurality of stages of nanofiltration membrane components which are connected in series in sequence, wherein the membrane configurations which can be used by the membrane components are flat plates, tubular, roll type and hollow fiber type, the nanofiltration membrane components which are connected in series in sequence can realize the long-term stable operation of the membrane components, and effectively control the problem of membrane pollution and the problem of membrane service life reduction caused by frequent regeneration of the membranes. The reverse osmosis mechanism 4 comprises a filter, a high-pressure water supply pump, an electric slow-opening door, a multi-stage reverse osmosis membrane module, a control valve and the like, solvent water permeates through the reverse osmosis membrane by applying pressure to the multi-stage reverse osmosis membrane module, the concentration and the reduction of salt water are realized, and the membrane module is cleaned when the standard water yield is reduced by 10% and the pressure drop is increased by 15%. The mass concentration of sodium chloride in the wastewater treated by the reverse osmosis mechanism 4 is stabilized between 6 and 8 percent, and when the bipolar membrane electrodialysis mechanism 6 treats the wastewater with the concentration, the bipolar membrane electrodialysis mechanism 6 can not cause high-load operation, and higher acid and alkali yield can be obtained.
On the basis of the technical scheme, more preferably, the nanofiltration mechanism 3 is reversely communicated with the triple box mechanism 1.
The nanofiltration mechanism 3 is communicated with the triple box mechanism 1 in a reverse direction, and divalent salt wastewater generated by the nanofiltration mechanism 3 can be discharged into the triple box mechanism 1 for continuous treatment.
On the basis of the technical scheme, further, the bipolar membrane electrodialysis mechanism 6 is respectively communicated with the acid liquor storage tank 9 and the alkali liquor storage tank 10; the bipolar membrane electrodialysis mechanism 6 is communicated with the resin adsorption mechanism 5 or the regulating tank 8; the bipolar membrane electrodialysis mechanism 6 is reversely communicated with the reverse osmosis mechanism 4, and the neutralization pond 7 is arranged on a reversely communicated passage.
When the bipolar membrane electrodialysis mechanism 6 operates, the volume ratio of the initial liquid of the salt chamber, the acid chamber and the alkali chamber in the mechanism is controlled to be 1:1:1, 2% NaOH solution is used as electrolyte, the circulation volume of circulating concentrated brine in the salt chamber in the mechanism is 10t/h, the circulation flow of circulating concentrated brine in the acid chamber and the alkali chamber in the mechanism is 10t/h, the treatment period of the salt-containing wastewater is 60min, and the generated acid alkali liquid is discharged to acid-base storage equipment or pumped into other equipment for recycling. After each batch of brine is circularly processed for 2 periods, the residual weak brine is discharged to a neutralization pond 7 for circular processing.
On the basis of the above technical solution, it is more preferable that the neutralization tank 7 is provided with a dosing component and an online pH monitor. The dosing component is arranged at the mouth of the neutralization tank 7 and used for controlling the dosing amount of the medicament, and the controller of the pH online monitor is arranged outside the neutralization tank 7, and the probe of the pH online monitor is arranged inside the neutralization tank 7 and is submerged in the liquid in the neutralization tank 7. The neutralization tank 7 can effectively buffer the problem that the concentration of hydrogen ions is increased due to ion back migration in the bipolar membrane electrodialysis process.
The desulfurization wastewater treatment system in the preferred technical scheme is used for treating desulfurization wastewater of a certain thermal power plant, and the specific treatment steps are as follows:
the desulfurization wastewater is pretreated by utilizing the triple box mechanism 1, and the desulfurization wastewater is subjected to neutralization, reaction, flocculation and other processes in sequence in the triple box mechanism 1. Adding slaked lime into a neutralization tank 7 of the triple box, and adjusting the pH value to about 9; adding a heavy metal chelating agent TMT-15 into a triple-box reaction tank, wherein the effective concentration of the heavy metal chelating agent TMT-15 is controlled to be about 14 percent, and the density of the heavy metal chelating agent TMT-15 is not less than 1.0g/cm3The residence time is about 40 min; and (3) adding a PAM flocculating agent into the triple-box flocculating tank, controlling the concentration to be 0.2%, and separating out clarified liquid after staying for 40min to the next process link.
Clear liquid in the triple box overflows to a chemical softening mechanism 2, 5 percent NaOH is added to remove magnesium ions in the softening process, the liquid caustic consumption is controlled according to the water quality of the wastewater, the pH value of the wastewater is finally controlled to be 11,adding Na again2CO3And controlling the concentration of the medicament to be 0.2%, continuously adding 0.3% flocculant PAM, and controlling the hydraulic retention time to be 50min until the hardness of clarified effluent is about 70 ppm.
The effluent of the chemical softening mechanism 2 is pumped into a nanofiltration mechanism 3, the nanofiltration mechanism 3 can further reduce the hardness of wastewater and separate divalent salt in the wastewater, and a two-stage nanofiltration roll-type membrane module is used in the mechanism, the maximum withstand pressure of the membrane module is 70bar, and the intercepted molecular weight is 300 Dalton. The operating pressure of the nanofiltration mechanism 3 is 2.0MPa, and the water inlet flow is 8m3The turbidity was controlled to 1.0 or less. When the desalination rate is obviously reduced and the pressure drop is obviously increased in the nanofiltration process, the membrane module is cleaned, and the cleaning solution comprises sodium tripolyphosphate, EDTA tetrasodium salt and the like. And divalent salt concentrated water generated by the nanofiltration mechanism 3 is pumped into the triple box mechanism 1 for circular treatment, and monovalent salt wastewater is pumped into the reverse osmosis mechanism 4.
The nanofiltration effluent is conveyed to a reverse osmosis mechanism 4, the reverse osmosis mechanism 4 applies pressure to enable solvent water to permeate a reverse osmosis membrane, so that the concentration and reduction of brine are realized, the mechanism uses two-stage polyamide membrane components, and the desalination rate is more than 98%. When the reverse osmosis mechanism 4 operates, the inflow rate is 5m3And h, the pressure is 0.3MPa, the brine treated by the reverse osmosis mechanism 4 is discharged into the regulating tank 8, and the concentration of the stabilized brine is about 6.5 percent. The fresh water produced by the reverse osmosis mechanism 4 is stored in a container ready for reuse in other processes. When the standard water yield is reduced by 10% and the pressure drop is increased by 15%, cleaning the membrane module.
The concentrated brine enters an adjusting tank 8, the mass concentration of the sodium chloride component of the concentrated brine is adjusted to be stable at 6-8%, the pH is controlled at 7-9, and the next process treatment is carried out when the conductivity reaches 80 ms/cm.
The salt water after being regulated to be stable by the regulating tank 8 is pumped into the resin adsorption mechanism 5, and 001 x 7 and CH-90 are selected as resin fillers. The pH value of the inlet water of the resin adsorption mechanism 5 is controlled to be about 8, and the flow rate is controlled to be 8 m/h. After resin adsorption treatment, the wastewater hardness is about 1 ppm.
Pumping the saline water after resin adsorption treatment into a bipolar membrane electrodialysis system by a magnetic pump, and controlling the inflow of water to be 6m3The initial liquid volumes of the acid chamber, the salt chamber and the alkali chamber are respectively set to be 5m in initial operation3The initial solution of the acid chamber and the alkali chamber of the bipolar membrane electrodialysis mechanism can use fresh water produced by a reverse osmosis system, and the electrode solution uses 3% NaOH solution. The treatment period of each batch of wastewater is 1 hour, the prepared acid-base solution is taken out after 1 hour, and the prepared acid-base solution can be reused in other processes.
Discharging the residual weak brine after the bipolar membrane electrodialysis circulation treatment into a neutralization tank 7, adding 1% of NaOH into the neutralization tank 7 until the pH value is stabilized to about 7, pumping the neutralized wastewater into a reverse osmosis mechanism 4 for recycling, wherein the used NaOH can be alkali liquor prepared by the bipolar membrane electrodialysis.
The wastewater treated by the desulfurization wastewater treatment method can realize zero discharge, and table 1 shows the detection results of the content of heavy metal components in the acid solution prepared by the invention.
Table 1 test results of heavy metal content in acid solution
Note: -is not detected
The data in the table 1 show that the heavy metal content of each component in the acid solution prepared by the desulfurization wastewater treatment method is lower, the arsenic content after monitoring is lower than 0.0001%, and the quality meets the qualified grade in the industrial synthetic hydrochloric acid standard in GB 320-2006. According to the invention, impurities in the wastewater can be effectively removed by utilizing the combined process, the overall service life and treatment efficiency of a subsequent bipolar membrane electrodialysis system are improved, zero discharge of desulfurization wastewater can be realized, and high-quality acid-base byproducts can be obtained.
As shown in figure 2, the utility model discloses a desulfurization waste water treatment process flow, the desulfurization waste water that thermal power plant wet flue gas desulfurization produced are in proper order through three headers, chemical softening, receive and strain, reverse osmosis treatment, and the play water after reverse osmosis treatment is adjusted the back through the equalizing basin, gets rid of impurity through the resin adsorption, prepares acid-base liquid by bipolar membrane electrodialysis at last, realizes the utilization of resources of waste water. And residual fresh water in the bipolar membrane electrodialysis process flows back to a reverse osmosis system through a neutralization tank for circular treatment, so that the wastewater treatment efficiency is improved. And the divalent salt-containing wastewater generated in the nanofiltration process flows back to the triple box for continuous treatment.
Finally, it should be noted that: the above embodiments are only used to illustrate the technical solution of the present invention, and not to limit the same; although the present invention has been described in detail with reference to the foregoing embodiments, it should be understood by those skilled in the art that: the technical solutions described in the foregoing embodiments may still be modified, or some or all of the technical features may be equivalently replaced; such modifications and substitutions do not depart from the spirit and scope of the present invention.
Claims (7)
1. A desulfurization wastewater treatment system capable of recycling resources is characterized by comprising a triple box mechanism (1), a chemical softening mechanism (2), a nanofiltration mechanism (3), a reverse osmosis mechanism (4), a resin adsorption mechanism (5), a bipolar membrane electrodialysis mechanism (6) and a neutralization tank (7);
the triple box mechanism (1), the chemical softening mechanism (2), the nanofiltration mechanism (3), the reverse osmosis mechanism (4), the resin adsorption mechanism (5) and the bipolar membrane electrodialysis mechanism (6) are communicated in sequence;
the bipolar membrane electrodialysis mechanism (6) is reversely communicated with the reverse osmosis mechanism (4), and the neutralization pond (7) is arranged on a reversely communicated passage.
2. The treatment system according to claim 1, wherein a conditioning tank (8) is provided between the reverse osmosis mechanism (4) and the resin adsorption mechanism (5), or between the resin adsorption mechanism (5) and the bipolar membrane electrodialysis mechanism (6).
3. The treatment system according to claim 2, wherein a stirrer, a conductivity meter, a turbidity meter and an on-line pH monitor are arranged in the conditioning tank (8).
4. The treatment system according to claim 3, wherein the nanofiltration mechanism (3) comprises a plurality of stages of nanofiltration membrane modules connected in series in sequence, and the reverse osmosis mechanism (4) comprises a plurality of stages of reverse osmosis membrane modules connected in series in sequence;
the chemical softening mechanism (2) is communicated with the first stage of the nanofiltration membrane component, the last stage of the nanofiltration membrane component is communicated with the first reverse osmosis membrane component, and the last stage of the reverse osmosis membrane component is communicated with the regulating tank (8) or the resin adsorption mechanism (5).
5. A treatment system according to claim 3, wherein the nanofiltration mechanism (3) is in reverse communication with the triple box mechanism (1).
6. The treatment system according to claim 3, wherein an acid liquid storage tank (9) and an alkali liquid storage tank (10) are communicated with the bipolar membrane electrodialysis mechanism (6); the bipolar membrane electrodialysis mechanism (6) is communicated with the resin adsorption mechanism (5) or the regulating tank (8); the bipolar membrane electrodialysis mechanism (6) is reversely communicated with the reverse osmosis mechanism (4), and the neutralization pond (7) is arranged on a reversely communicated passage.
7. A treatment system according to claim 3, wherein the neutralization tank (7) is provided with an administration component and an on-line pH monitor.
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Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN114560722A (en) * | 2022-02-28 | 2022-05-31 | 同济大学 | Method for recycling kitchen waste anaerobic fermentation liquor |
| US11502323B1 (en) | 2022-05-09 | 2022-11-15 | Rahul S Nana | Reverse electrodialysis cell and methods of use thereof |
| US11502322B1 (en) | 2022-05-09 | 2022-11-15 | Rahul S Nana | Reverse electrodialysis cell with heat pump |
| US11855324B1 (en) | 2022-11-15 | 2023-12-26 | Rahul S. Nana | Reverse electrodialysis or pressure-retarded osmosis cell with heat pump |
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Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN114560722A (en) * | 2022-02-28 | 2022-05-31 | 同济大学 | Method for recycling kitchen waste anaerobic fermentation liquor |
| US11502323B1 (en) | 2022-05-09 | 2022-11-15 | Rahul S Nana | Reverse electrodialysis cell and methods of use thereof |
| US11502322B1 (en) | 2022-05-09 | 2022-11-15 | Rahul S Nana | Reverse electrodialysis cell with heat pump |
| US11563229B1 (en) | 2022-05-09 | 2023-01-24 | Rahul S Nana | Reverse electrodialysis cell with heat pump |
| US11611099B1 (en) | 2022-05-09 | 2023-03-21 | Rahul S Nana | Reverse electrodialysis cell and methods of use thereof |
| US11699803B1 (en) | 2022-05-09 | 2023-07-11 | Rahul S Nana | Reverse electrodialysis cell with heat pump |
| US11855324B1 (en) | 2022-11-15 | 2023-12-26 | Rahul S. Nana | Reverse electrodialysis or pressure-retarded osmosis cell with heat pump |
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