CN105800885B - The resource utilization of high-concentration hardly-degradable salt-containing organic wastewater utilizes processing system - Google Patents
The resource utilization of high-concentration hardly-degradable salt-containing organic wastewater utilizes processing system Download PDFInfo
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Abstract
A kind of resource utilization of high-concentration hardly-degradable salt-containing organic wastewater utilizes processing system, including crystallization fluorine removal reactor, comprehensive wastewater conditioning tank, biochemical treatment system, advanced oxidation unit, filter element, ultrafiltration apparatus, resin softening plant, reverse osmosis unit, concentrated type electrodialysis plant, nanofiltration device, the first bipolar membrane electrodialysis device and the second bipolar membrane electrodialysis device.Present invention optimizes kinds of processes combinations, can remove organic matter and inorganic salts difficult to degrade in waste water step by step, realize that the resource utilization of high-concentration hardly-degradable salt-containing organic wastewater utilizes on the basis of " near-zero release "；The production water rate of recovery generated after processing can be used as the moisturizing with water and recirculated cooling water of production technology up to 95% or more；This invention ensures that biochemical reaction influent quality requires；By biochemical treatment and advanced oxidation reaction, the risk of subsequent desalination system organic pollution is effectively reduced.
Description
Technical field
The present invention is that a kind of resource utilization of high-concentration hardly-degradable salt-containing organic wastewater utilizes processing system and processing work
Skill belongs to field of waste water treatment.More particularly to a kind of physics for this high-concentration hardly-degradable salt-containing organic wastewater
Processing, chemical treatment, biological treatment, film advanced treating integrated treatment process, it is intended to using the system in " near-zero release "
On the basis of realize high-concentration hardly-degradable salt-containing organic wastewater resource utilization utilize.
Background technique
Sanitary sewage and industrial wastewater are the primary pollution source of China's water body.Currently, sanitary sewage disposal technology has become
In maturation, and the processing of industrial wastewater is not solved thoroughly also, especially petrochemical industry, coal chemical industry, metallurgy, printing and dyeing, system
The processing technique for the high-concentration hardly-degradable salt-containing organic wastewater that the industries such as medicine, papermaking are discharged in process of production is still immature.It should
Waste water quality feature is mainly manifested in the following aspects: (1) organic pollutant concentration is high, and general COD is more than 2000mg/L, very
To can achieve tens of thousands of mg/litres；(2) difficult to degrade, wastewater biodegradability is poor, its ratio of BOD/COD will be generally less than 0.3, very
To lower；(3) salt content is high, and the salt content in usual waste water is higher than 3000mg/L；(4) pollutant component is complicated, organic wastewater
In usually contain the noxious material difficult to degrade such as aromatic compound, heterocyclic compound, sulfide, cyanide, heavy metal；(5) color
Degree is high, and there are peculiar smell, are affected to surrounding enviroment.
Since hardly degraded organic substance content is greatly in this kind of waste water and the toxicity of the substances such as polycyclic aromatic hydrocarbon, BaP is big, so that
Single biologic treating technique, physical chemistry processing technique are difficult to realize the qualified discharge of this kind of waste water.Investigation shows petroleum
The industries water consumption such as work, coal chemical industry, metallurgy, printing and dyeing, pharmacy, papermaking is big, if being recycled using advanced treatment process this kind of
Waste water can not only mitigate pollution on the environment, moreover it is possible to waste water be turned waste into wealth, recycled, and then reduce fresh water
Dosage, considerable economic benefit is brought to enterprise.However membrane system is also easy to produce in conventional advanced treatment process operational process
The problem of organic pollution of system and inorganic salts fouling, so that the technique is difficult for long-term stable operation.In addition, conventional depth
The rate of recovery of reason technique waste water is low, concentrated water yield is big, if a large amount of pollutant is concentrated in direct emission in concentrated water, will cause serious
Environmental pollution.
Therefore, in order to realize waste water high-recovery, process system " near-zero release ", eliminate concentrated water, waste residue and waste water
Pollution to environment proposes processing system and treatment process that a set of whole process, efficient resource utilization utilize.
Summary of the invention
It is an object of the invention to design a kind of resource utilization benefit of novel high-concentration hardly-degradable salt-containing organic wastewater
With processing system, solve the above problems.
To achieve the goals above, The technical solution adopted by the invention is as follows:
A kind of resource utilization of high-concentration hardly-degradable salt-containing organic wastewater utilizes processing system, comprising:
Crystallization fluorine removal reactor: defluorinating agent is wherein added and stirs, for high-concentration hardly-degradable saliferous to be processed to have
Fluorine ion in machine waste water is removed in the form of sediment, to reduce the fouling risk that subsequent membranous system is generated by calcirm-fluoride；
Comprehensive wastewater conditioning tank: it is removed for the uniformly water quality of the water outlet of the crystallization fluorine removal reactor, the adjusting crystallization
The water of the water outlet of fluorine reactor；
Biochemical treatment system: for the water outlet of the comprehensive wastewater conditioning tank, the drop of COD is realized under the action of microorganism
Solution, the synchronous removal for realizing nitrogen and phosphorus；
Advanced oxidation unit: it for the water outlet of the biochemical treatment system, removes difficult to degrade in the biochemical treatment system
Organic matter, reduce the risk that subsequent desalination system generates organic pollution；
Filter element: for the water outlet of the advanced oxidation unit to be filtered, delivery turbidity is reduced；
Ultrafiltration apparatus: for further removing suspended matter, colloid, the microorganism etc. in the water outlet of the filter element；
Resin softening plant: for the water outlet of the ultrafiltration apparatus, calcium ion and magnesium ion is removed, subsequent desalination system is reduced
The risk of system inorganic salts fouling；The calcium chloride and magnesium chloride contained in the acid-basic regenerated waste liquids in water of the resin softening plant, reflux
It is used to the crystallization fluorine removal reactor as defluorinating agent；
Reverse osmosis unit: for the water outlet of the resin softening plant and the production water of the concentrated type electrodialysis plant, drop
Low inorganic salt concentration therein, while removing remaining organic matter；The production water of the reverse osmosis unit is as product water reuse；
Concentrated type electrodialysis plant: for the concentrated water of the reverse osmosis unit to be further concentrated；The concentrated type electric osmose
The production water of analysis apparatus is back to the reverse osmosis unit and further recycles；
Nanofiltration device: for separating sulfate ion in the concentrated water of the concentrated type electrodialysis plant and chloride ion；
First bipolar membrane electrodialysis device: the nanofiltration for containing chloride ion for the nanofiltration device produces water, will be with NaCl
Main salting liquid is converted to hydrochloric acid solution and sodium hydroxide solution；
Second bipolar membrane electrodialysis device: containing the nanofiltration concentrated water of sulfate ion for the nanofiltration device, will be with
Na2SO4Based on salting liquid be converted to sulfuric acid solution and sodium hydroxide solution.
It preferably, further include oil separator and flotation tank, high-concentration hardly-degradable salt-containing organic wastewater to be processed initially enters
After the oil separator and the flotation tank, the crystallization fluorine removal reactor is entered back into.
It preferably, further include sludge-tank and sludge dewatering equipment, the flotation tank, the crystallization fluorine removal reactor and the life
The sediment changed in processing system enters the sludge-tank, and then after sludge dewatering equipment dehydration, sludge is transported.
Preferably, the filter element includes the combination of manganese sand filter or more medium filter or both；
By the iron ion and manganese ion in aeration removal waste water in the manganese sand filter, and pass through the manganese sand filter
In manganese sand filtering material primary filtration remove partial suspended thing；
The more medium filter carries out fine filtering, filters in the more medium filter equipped with quartz sand and anthracite
Material removes fine suspension and reduces delivery turbidity；
The partial size of manganese sand filtering material in the manganese sand filter is 1-2mm；
The partial size of the quartz sand and ANTHRACITE FILTER MEDIA that are equipped in the more medium filter is 0.8-1.2mm.
It preferably, further include manganese sand discharge bay, then the water outlet of the manganese sand filter first passes through the manganese sand discharge bay again
Into next device；
It further include multimedium discharge bay, then the water outlet of the more medium filter first passes through the multimedium discharge bay again
Into next device；
It further include bio-chemical effluent pond, the water outlet of the biochemical treatment system first passes through the bio-chemical effluent pond and then enters back into
Next device；
It further include ultra-filtration water pond, the water outlet of the ultrafiltration apparatus first passes through the ultra-filtration water pond and then enters back into next
A device；
It further include softening discharge bay, the water outlet of the resin softening plant first passes through the softening discharge bay and then enters back into
Next device；
Further include reverse osmosis water outlet pond, the water outlet of the reverse osmosis unit first pass through the reverse osmosis water outlet pond then again into
Enter next device.
It preferably, further include targeting catalyst oxidation reactor and fiber ball filter, the concentrated water of the reverse osmosis unit is first
It is introduced into the targeting catalyst oxidation reactor, removes the hardly degraded organic substance being concentrated in concentrated water；Fiber ball filter is entered back into,
It carries out deep layer and cuts dirt；Then the concentrated type electrodialysis plant is entered back into further to be concentrated.
Preferably, the defluorinating agent is added in the crystallization fluorine removal reactor, and be sufficiently stirred so that the high concentration
Salt-containing organic wastewater difficult to degrade is centrifuged after forming crystal, removes fluorine ion therein with solid forms；The fluorine removal
Agent is one or both of calcium chloride or magnesium chloride.
Preferably, anti-comprising improvement Fenton oxidation reaction system and/or targeting catalysis oxidation in the advanced oxidation unit
Answer system；
The improvement Fenton oxidation reaction system adds ferrous sulfate and hydrogen peroxide under conditions of not acid adding, has dirt
Object degradation capability is contaminated, also reduction reagent consumption amount and sludge yield；
Filling needle is to the catalyst of different quality feature in the described targeting catalytic oxidation system, and is passed through ozone,
The hydroxyl radical free radical for making ozone accelerated decomposition generation strong oxidizing property by the inducing action of catalyst, the feature in waste water is dirty
Dye object thoroughly decomposes.
Preferably, the resin softening plant is using sodium form cation exchange resin, Hydrogen Subacidity cation exchange tree
One of rouge or chelating resin form；
The nanofiltration device is retained using selectivity of the nanofiltration membrane to ion, and sulfate ion and chloride ion are separated
It opens；
The hydrochloric acid solution generated in first bipolar membrane electrodialysis device is for resin in the resin softening plant
Regeneration, and for the chemical cleaning including the ultrafiltration apparatus, concentrated type electrodialysis plant；
The sulfuric acid solution generated in the second generation bipolar membrane electrodialysis device is for the high-concentration hardly-degradable saliferous
The resource utilization of organic wastewater utilizes the adjusting of the system pH in treatment process；
The hydroxide generated in first bipolar membrane electrodialysis device and the second generation bipolar membrane electrodialysis device
Money of the sodium solution for the regeneration of resin in the resin softening plant and for the high-concentration hardly-degradable salt-containing organic wastewater
Sourceization recycles the adjusting of the system pH in treatment process, and for filling including the ultrafiltration apparatus, concentrated type electrodialysis
Chemical cleaning including setting.
It preferably, further include the cartridge filter required for meeting the water inlet of reverse osmosis unit, the resin softening dress
The water outlet set enters back into the reverse osmosis unit after the cartridge filter；
It further include self-cleaning filter, after the water inlet of the ultrafiltration apparatus will first pass through the self-cleaning filter, then into
Enter the ultrafiltration apparatus.
So-called high-concentration hardly-degradable salt-containing organic wastewater refers to that organic pollutant concentration is high in the present invention, and general COD is super
Cross 2000mg/L, it might even be possible to reach tens of thousands of mg/litres；Wastewater biodegradability is poor, its ratio of BOD/COD will be generally less than 0.3,
It is even lower；Salt content is high, and the salt content in usual waste water is higher than 3000mg/L；Pollutant component is complicated, leads in organic wastewater
Often containing noxious materials difficult to degrade such as aromatic compound, heterocyclic compound, sulfide, cyanide, heavy metals；Coloration is high, deposits
In peculiar smell, the industrial wastewater being affected to surrounding enviroment.
Comprehensive wastewater conditioning tank mainly utilizes pool capacity, pond structure (baffle plate, blender etc.) uniform water in the present invention
Matter, equilibrium water amount.
By-product has been obtained to concentrated water advanced treating using the group technology of nanofiltration and bipolar membrane electrodialysis device in the present invention
Object hydrochloric acid, sulfuric acid and sodium hydroxide solution.The chemistry that hydrochloric acid solution can be used for the devices such as resin regeneration and ultrafiltration, electrodialysis is clear
It washes；Sulfuric acid solution can be used for system pH adjusting；And sodium hydroxide solution cannot be only used for resin regeneration, the adjusting of system pH may be used also
It is directly used in the chemical cleaning of ultrafiltration, electrodialysis plant, the inside circulation and resource utilization for realizing concentrated water in system utilize.
Bipolar membrane electrodialysis device generates in the present invention hydrochloric acid and sodium hydroxide are used for the regeneration of resin, can not only reach
Good regeneration effect, and the composition in its regenerated liquid is with CaCl2、MgCl2Based on, and can be used as in crystallization fluorine removal reactor
Defluorinating agent, realize regeneration liquid waste inside circulation and resource utilization utilize, achieved the purpose that the treatment of wastes with processes of wastes against one another.
The purpose of the present invention is optimize a variety for the treatment of process to couple to form the resource of high-concentration hardly-degradable salt-containing organic wastewater
Change and recycles processing system and treatment process.Not external sewage effluent in whole flow process, producing water can be used as recirculated cooling water benefit
Water and process water are back to different production units, and dross, the sludge of generation form mud cake after being dehydrated, can be used as Lightweight ceramic
The raw material of the building materials such as grain, eco-cement, brick.
The resource utilization of high-concentration hardly-degradable salt-containing organic wastewater includes following step using the treatment process of processing system
It is rapid:
(1) pretreating process: high-concentration hardly-degradable salt-containing organic wastewater initially enters oil separator, flotation tank, removes waste water
In oils and solid suspension.Flotation tank water outlet enters crystallization fluorine removal reactor, and fluorine removal is added in crystallization fluorine removal reactor
Agent is simultaneously sufficiently stirred, formed the biggish crystal of particle after Natural zeolite is removed in the form of sediment, with reduce subsequent membranous system because
The fouling risk that calcirm-fluoride generates, the water outlet of crystallization fluorine removal reactor enter the tune that comprehensive wastewater conditioning tank carries out water quality and quantity
Section.
(2) biochemical processing process: the water outlet of comprehensive wastewater conditioning tank is promoted to biochemical treatment system through pump, in the work of microorganism
With the lower degradation for realizing most COD, the removal for realizing nitrogen, phosphorus furthermore should be synchronized in the process, and biochemical treatment system water outlet flows into
Into bio-chemical effluent pond.
(3) depth pretreating process: the water outlet of bio-chemical effluent pond is promoted through pump, into advanced oxidation unit, removes department of biochemistry
It is difficult to the organic matter degraded in system, reduces the organic pollution risk that subsequent desalination system generates.Wherein advanced oxidation unit packet
Include one of the reaction of improvement Fenton oxidation, targeting catalytic oxidation.The characteristics of improveing Fenton oxidation technique is in not acid adding
Under conditions of ferrous sulfate and hydrogen peroxide are added into reactor, not only realize stronger contaminant degradation ability, also significantly
Reduce reagent consumption amount and sludge yield.And the characteristics of targeting catalytic oxidation be into reactor filling needle to specific
The catalyst of water quality type selecting, and it is passed through ozone, make ozone accelerated decomposition generate strong oxidizing property by the inducing action of catalyst
Hydroxyl radical free radical, the characteristic contamination in waste water is thoroughly decomposed.
The water outlet of advanced oxidation unit enters manganese sand filter, by the Fe and Mn in aeration removal waste water, additionally may be used
To remove partial suspended thing by the partial size in manganese sand filter for the manganese sand filtering material primary filtration of 1-2mm.Manganese sand filter water outlet warp
Pump is lifted into more medium filter fine filtering, and more medium filter is equipped with the quartz sand that partial size is 0.8-1.2mm and smokelessly
Coal filtering material reduces delivery turbidity for removing fine suspension.
(4) advanced treatment process: more medium filter water outlet further removes oil removal and colloid through self-cleaning filter
Enter ultrafiltration apparatus after equal pollutants, ultrafiltration apparatus can remove the almost all such as suspended matter, colloid, microorganism.Ultrafiltration apparatus
Water outlet enter resin softening plant, resin softening plant is handed over using sodium form cation exchange resin, Hydrogen Subacidity cation
One of resin or chelating resin form are changed, most calcium and magnesium ion can be removed after resin softens, after reduction
The risk of continuous desalination system inorganic salts fouling.Main ingredient is that calcium chloride and magnesium chloride therefore can be straight in acid-basic regenerated waste liquids in water
It connects to be back in crystallization fluorine removal reactor as defluorinating agent and use.The water outlet of resin softening plant is promoted to security personnel's filtering through pump
Device, to meet the water inlet requirement of reverse osmosis unit, subsequently into reverse osmosis unit.Reverse osmosis unit can reduce inorganic in waste water
Salinity, while remaining organic matter is removed, guarantee that effluent quality meets quality of reused water requirement.Reverse osmosis unit produces water and enters
Reuse pool, as product water reuse.
(5) concentrated water treatment process: the concentrated water of reverse osmosis unit enters reverse osmosis concentrated pond, is promoted to targeting catalysis oxygen through pump
Change reactor, removes the hardly degraded organic substance being concentrated in concentrated water.Water outlet enters fiber ball filter from top to bottom, by fibrous nodules
Filtrate carries out deep layer and cuts dirt.Fiber ball filter water outlet is promoted to concentrated type electrodialysis plant through pump and is further concentrated.It is concentrated
The water inlet that the production water of type electrodialysis plant is back to reverse osmosis unit further recycles, and concentrated water by front end pretreatment,
After biochemical treatment and advanced treatment process, suspended matter, colloid and calcium and magnesium ion etc. are removed substantially, main component
With Na2SO4Based on the inorganic salts such as NaCl.The concentrated water of concentrated type electrodialysis plant enters nanofiltration device, since nanofiltration membrane is to multivalence
The rejection of ion will be far longer than monovalention, therefore, can separate most of sulfate radical and chloride ion.Contain chloride ion
Nanofiltration produce water enter bipolar membrane electrodialysis device, the centrifugation by Bipolar Membrane is converted to the salting liquid based on NaCl
Hydrochloric acid and sodium hydroxide solution；And the nanofiltration concentrated water containing sulfate ion also passes through bipolar membrane electrodialysis device, it will be with Na2SO4
Based on salting liquid be converted to sulfuric acid and sodium hydroxide.The hydrochloric acid solution that bipolar membrane electrodialysis device generates can be used for resin regeneration
And the chemical cleaning of the devices such as ultrafiltration, electrodialysis；The sulfuric acid solution of generation can be used for the adjusting of system pH；The hydroxide of generation
Sodium solution can be used for the chemical cleaning of resin regeneration, the adjusting of system pH and ultrafiltration, electrodialysis plant.Simultaneously extra acid,
Alkali can be sold to the not high producer of soda acid quality requirements.
Beneficial effects of the present invention can be summarized as follows:
(1) the present invention provides a kind of resource utilizations of high-concentration hardly-degradable salt-containing organic wastewater using processing system and
Treatment process, system optimization kinds of processes combination, can remove organic matter and inorganic salts difficult to degrade in waste water step by step,
Realize that the resource utilization of high-concentration hardly-degradable salt-containing organic wastewater utilizes on the basis of " near-zero release ".
(2) for the production water rate of recovery generated after present invention process processing up to 95% or more, can be used as production technology uses water
And the moisturizing of recirculated cooling water.
(3) system by front end pretreatment removal waste water in suspended matter and part COD, ensure that biochemical reaction into
Water water quality requirement；Removal by crystallization fluorine removal reactor to the removing and resin softening plant of fluorine ion to calcium and magnesium ion, greatly
The risk of subsequent desalination system inorganic salts fouling is reduced greatly；By biochemical treatment and advanced oxidation reaction, after effectively reducing
The risk of continuous desalination system organic pollution.By the combined treatment of process above unit, guarantee entire process system especially
Advanced treatment process is run steadily in the long term.
(4) group technology for the nanofiltration and bipolar membrane electrodialysis device that the present invention uses obtains concentrated water advanced treating
By-product hydrochloric acid, sulfuric acid and sodium hydroxide solution.Hydrochloric acid solution can be used for the change of the devices such as resin regeneration and ultrafiltration, electrodialysis
Learn cleaning；Sulfuric acid solution can be used for system pH adjusting；And sodium hydroxide solution cannot be only used for the adjusting of resin regeneration, system pH
The chemical cleaning that also can be directly used for ultrafiltration, electrodialysis plant realizes the inside circulation and resource utilization of concentrated water in system
It utilizes.
(5) by-product hydrochloric acid and sodium hydroxide are used for the regeneration of resin, can not only reach good regeneration effect, Er Qieqi
Composition in regenerated liquid is with CaCl2、MgCl2Based on, and can be used as the defluorinating agent in crystallization fluorine removal reactor, realize regenerated
The inside circulation and resource utilization of liquid utilize, and have achieved the purpose that the treatment of wastes with processes of wastes against one another.
(6) aggregation system of the present invention has high treating effect, stable, small accommodation area, impact resistance ability strong, automatic
The advantages that change degree is high, easy to operate.
Detailed description of the invention
Fig. 1 is that the resource utilization of high-concentration hardly-degradable salt-containing organic wastewater of the present invention utilizes the treatment process of processing system
A kind of embodiment flow chart.
Fig. 2 is that the resource utilization of high-concentration hardly-degradable salt-containing organic wastewater of the present invention utilizes the treatment process of processing system
Another embodiment flow chart.
Specific embodiment
In order to which the technical problems, technical solutions and beneficial effects solved by the present invention is more clearly understood, below in conjunction with
Accompanying drawings and embodiments, the present invention will be described in further detail.It should be appreciated that specific embodiment described herein only to
It explains the present invention, is not intended to limit the present invention.
A kind of resource utilization of high-concentration hardly-degradable salt-containing organic wastewater as shown in Fig. 1 to 2 utilizes processing system, packet
It includes:
Crystallization fluorine removal reactor: defluorinating agent is wherein added and stirs, for high-concentration hardly-degradable saliferous to be processed to have
Fluorine ion in machine waste water is removed in the form of sediment, to reduce the fouling risk that subsequent membranous system is generated by calcirm-fluoride；
Comprehensive wastewater conditioning tank: it is removed for the uniformly water quality of the water outlet of the crystallization fluorine removal reactor, the adjusting crystallization
The water of the water outlet of fluorine reactor；
Biochemical treatment system: for the water outlet of the comprehensive wastewater conditioning tank, the drop of COD is realized under the action of microorganism
Solution, the synchronous removal for realizing nitrogen and phosphorus；
Advanced oxidation unit: it for the water outlet of the biochemical treatment system, removes difficult to degrade in the biochemical treatment system
Organic matter, reduce the risk that subsequent desalination system generates organic pollution；
Filter element: for the water outlet of the advanced oxidation unit to be filtered, delivery turbidity is reduced；
Ultrafiltration apparatus: for further removing suspended matter, colloid, the microorganism etc. in the water outlet of the filter element；
Resin softening plant: for the water outlet of the ultrafiltration apparatus, calcium ion and magnesium ion is removed, subsequent desalination system is reduced
The risk of system inorganic salts fouling；The calcium chloride and magnesium chloride contained in the acid-basic regenerated waste liquids in water of the resin softening plant, reflux
It is used to the crystallization fluorine removal reactor as defluorinating agent；
Reverse osmosis unit: for the water outlet of the resin softening plant and the production water of the concentrated type electrodialysis plant, drop
Low inorganic salt concentration therein, while removing remaining organic matter；The production water of the reverse osmosis unit is as product water reuse；
Concentrated type electrodialysis plant: for the concentrated water of the reverse osmosis unit to be further concentrated；The concentrated type electric osmose
The production water of analysis apparatus is back to the reverse osmosis unit and further recycles；
Nanofiltration device: for separating sulfate ion in the concentrated water of the concentrated type electrodialysis plant and chloride ion；
First bipolar membrane electrodialysis device: the nanofiltration for containing chloride ion for the nanofiltration device produces water, will be with NaCl
Main salting liquid is converted to hydrochloric acid solution and sodium hydroxide solution；
Second bipolar membrane electrodialysis device: containing the nanofiltration concentrated water of sulfate ion for the nanofiltration device, will be with
Na2SO4Based on salting liquid be converted to sulfuric acid solution and sodium hydroxide solution.
It preferably, further include oil separator and flotation tank, high-concentration hardly-degradable salt-containing organic wastewater to be processed initially enters
After the oil separator and the flotation tank, the crystallization fluorine removal reactor is entered back into.
It preferably, further include sludge-tank and sludge dewatering equipment, the flotation tank, the crystallization fluorine removal reactor and the life
The sediment changed in processing system enters the sludge-tank, and then after sludge dewatering equipment dehydration, sludge is transported.
In more preferred embodiment, the filter element includes manganese sand filter or more medium filter or both
Combination；
By the iron ion and manganese ion in aeration removal waste water in the manganese sand filter, and pass through the manganese sand filter
In manganese sand filtering material primary filtration remove partial suspended thing；
The more medium filter carries out fine filtering, filters in the more medium filter equipped with quartz sand and anthracite
Material removes fine suspension and reduces delivery turbidity；
The partial size of manganese sand filtering material in the manganese sand filter is 1-2mm；
The partial size of the quartz sand and ANTHRACITE FILTER MEDIA that are equipped in the more medium filter is 0.8-1.2mm.
It in more preferred embodiment, further include manganese sand discharge bay, the water outlet of the manganese sand filter first passes through the manganese
Then sand discharge bay enters back into next device；
It further include multimedium discharge bay, then the water outlet of the more medium filter first passes through the multimedium discharge bay again
Into next device；
It further include bio-chemical effluent pond, the water outlet of the biochemical treatment system first passes through the bio-chemical effluent pond and then enters back into
Next device；
It further include ultra-filtration water pond, the water outlet of the ultrafiltration apparatus first passes through the ultra-filtration water pond and then enters back into next
A device；
It further include softening discharge bay, the water outlet of the resin softening plant first passes through the softening discharge bay and then enters back into
Next device；
Further include reverse osmosis water outlet pond, the water outlet of the reverse osmosis unit first pass through the reverse osmosis water outlet pond then again into
Enter next device.
It in more preferred embodiment, further include targeting catalyst oxidation reactor and fiber ball filter, the reverse osmosis
The concentrated water of saturating device initially enters the targeting catalyst oxidation reactor, removes the hardly degraded organic substance being concentrated in concentrated water；Again into
Enter fiber ball filter, carries out deep layer and cut dirt；Then the concentrated type electrodialysis plant is entered back into further to be concentrated.
In more preferred embodiment, the defluorinating agent is added in the crystallization fluorine removal reactor, and be sufficiently stirred
So that the high-concentration hardly-degradable salt-containing organic wastewater is centrifuged after forming crystal, fluorine therein is removed with solid forms
Ion；The defluorinating agent is one or both of calcium chloride or magnesium chloride.
In more preferred embodiment, in the advanced oxidation unit comprising improvement Fenton oxidation reaction system and/or
Target catalytic oxidation system；
The improvement Fenton oxidation reaction system adds ferrous sulfate and hydrogen peroxide under conditions of not acid adding, has dirt
Object degradation capability is contaminated, also reduction reagent consumption amount and sludge yield；
Filling needle is to the catalyst of different quality feature in the described targeting catalytic oxidation system, and is passed through ozone,
The hydroxyl radical free radical for making ozone accelerated decomposition generation strong oxidizing property by the inducing action of catalyst, the feature in waste water is dirty
Dye object thoroughly decomposes.
In more preferred embodiment, the resin softening plant uses sodium form cation exchange resin, Hydrogen weak acid
Property one of cation exchange resin or chelating resin form；
The nanofiltration device is retained using selectivity of the nanofiltration membrane to ion, and sulfate ion and chloride ion are separated
It opens；
The hydrochloric acid solution generated in first bipolar membrane electrodialysis device is for resin in the resin softening plant
Regeneration, and for the chemical cleaning including the ultrafiltration apparatus, concentrated type electrodialysis plant；
The sulfuric acid solution generated in the second generation bipolar membrane electrodialysis device is for the high-concentration hardly-degradable saliferous
The resource utilization of organic wastewater utilizes the adjusting of the system pH in treatment process；
The hydroxide generated in first bipolar membrane electrodialysis device and the second generation bipolar membrane electrodialysis device
Money of the sodium solution for the regeneration of resin in the resin softening plant and for the high-concentration hardly-degradable salt-containing organic wastewater
Sourceization recycles the adjusting of the system pH in treatment process, and for filling including the ultrafiltration apparatus, concentrated type electrodialysis
Chemical cleaning including setting.
It in more preferred embodiment, further include the cartridge filter required for meeting the water inlet of reverse osmosis unit,
The water outlet of the resin softening plant enters back into the reverse osmosis unit after the cartridge filter；
It further include self-cleaning filter, after the water inlet of the ultrafiltration apparatus will first pass through the self-cleaning filter, then into
Enter the ultrafiltration apparatus.
Embodiment 1:
Certain oil plant brine waste is handled using the integrated process flow in the method for the present invention attached drawing 1, water quality refers to
It marks as follows:
| Serial number | Project | Unit | Influent quality |
| 1 | CODCr | mg/L | ≤2200 |
| 2 | NH3-N | mg/L | ≤120 |
| 3 | Chloride ion | mg/L | ≤550 |
| 4 | Turbidity | NTU | ≤200 |
| 5 | Total hardness is (with CaCO3Meter) | mg/L | ≤350 |
| 6 | Total dissolved solid (TDS) | mg/L | ≤5500 |
| 7 | pH | - | 6~9 |
The system the following steps are included:
A, pretreating process
Waste water initially enters crystallization fluorine removal reactor and is pre-processed.By pretreatment, it is outstanding to remove useless water part solid
Floating object, organic matter and fluorine ion etc..
Pretreatment water outlet: turbidity≤130NTU, COD≤1700mg/L, water outlet flow into comprehensive wastewater conditioning tank and carry out water quality
The adjusting of water.
B, biochemical processing process
Biochemical processing process unit uses anaerobic- anoxic- oxic (A2O) technique carries out COD to waste water and nitrogen, phosphorus is gone
It removes.
By biochemical treatment unit, COD≤170mg/L of waste water, ammonia nitrogen≤5mg/L.
C, depth pretreating process
Biochemistry pool water outlet enters improvement Fenton oxidation reactor, occurs after adding ferrous sulfate and hydrogen peroxide in the reactor
Oxidation reaction removes most hardly degraded organic substance.After advanced oxidation reaction, COD≤60mg/L.Water outlet adds NaOH
Solution adjusts pH to 7.5 or so, is filtered into more medium filter.
After multi-medium filtering, turbidity≤5.0NTU in waste water.
D, advanced treatment process
More medium filter water outlet successively carries out depth by ultrafiltration apparatus, resin softening plant and reverse osmosis unit
Reason.Ultrafiltration membrane uses external pressing type hollow fibrous membrane element, intake pressure 0.3MPa, ultrafiltration apparatus delivery turbidity≤1NTU, SDI value
≤3.Ultrafiltration apparatus water outlet enters resin softening plant, which uses chelating resin, and the calcium and magnesium ion removed in waste water reduces
The hardness of water goes out the water hardness≤10mg/L to guarantee the normal operation of reverse osmosis membrane.Reverse osmosis unit uses antipollution reverse osmosis
Permeable membrane, operating pressure 1.5MPa of intaking, the rate of recovery 70%.
Reverse osmosis unit effluent quality is as follows: COD≤20mg/L, TDS≤220mg/L, chloride ion≤35mg/L, hardness≤
2mg/L, ammonia nitrogen≤0.5mg/L, turbidity≤0.1NTU, pH value 7.2~7.5, water quality indicator meet " industrial circulating cooling water processing
Design specification " requirement can reuse.
E, concentrated water treatment process
The concentrated water water quality indicator of reverse osmosis unit are as follows: COD≤160mg/L, conductivity≤25730 μ S/cm, chloride ion≤
1750mg/L, hardness≤29mg/L, turbidity≤0.1NTU.
The concentrated water of reverse osmosis unit enters concentrated type electrodialysis plant, and the concentrated type electrodialysis plant used is vertical knot
Structure, intake pressure≤0.4MPa, after the concentrated type electrodialysis process of concentrated water, the rate of recovery reaches 70%, salt rejection rate 75%, concentrated water electricity
Conductance≤70000 μ S/cm produces water conductivity≤6400 μ S/cm.The production water of concentrated type electrodialysis plant is back to feed water by reverse osmosis
Mouth further recycling, is used as product water reuse after reverse osmosis membrane is desalinated.The concentrated water of the concentrated type electrodialysis plant enters nanofiltration
Device retains the selectivity of ion using nanofiltration membrane so that chloride ion and sulfate ion separate in waste water, the film pair
The rejection of sulfate ion reaches 98% or more.Nanofiltration containing chloride ion produces water and enters the first bipolar membrane electrodialysis device,
Salting liquid based on NaCl is converted into hydrochloric acid and sodium hydroxide solution, conversion ratio reach 95%；And contain sulfate ion
Nanofiltration concentrated water enter the second bipolar membrane electrodialysis device, will be with Na2SO4Sulfuric acid is converted into for main salting liquid and sodium hydroxide is molten
Liquid, conversion ratio 93%.The hydrochloric acid that bipolar membrane electrodialysis device generates can be used for the devices such as resin regeneration and ultrafiltration, electrodialysis
Chemical cleaning；The sulfuric acid of generation can be used for the adjusting of system pH；The sodium hydroxide solution of generation can be used for resin regeneration, system
The adjusting and ultrafiltration of pH, electrodialysis plant chemical cleaning.Extra hydrochloric acid solution, sulfuric acid solution and sodium hydroxide solution is used
In the not high soda acid purposes of quality requirements.
Dross, the sludge generated in the system forms mud cake after being dehydrated, and can be used as light ceramic, eco-cement, brick etc.
The raw material of building materials.
Effluent quality index reaches the requirement of " Code for design of industrial recirculating cooling water treatment ", and specific data are as follows:
| Serial number | Project | Unit | Effluent quality | GB 50050-2007 design value |
| 1 | CODCr | mg/L | ≤20 | ≤30 |
| 2 | NH3-N | mg/L | ≤0.5 | ≤5 |
| 3 | Chloride ion | mg/L | ≤35 | ≤250 |
| 4 | Turbidity | NTU | ≤0.1 | ≤5 |
| 5 | Total hardness is (with CaCO3Meter) | mg/L | ≤2 | ≤250 |
| 6 | Dissolubility amounts to solid) body (TDS) | mg/L | ≤220 | ≤1000 |
| 7 | pH | - | 7.2~7.5 | 7.0~8.5 |
Note: GB 50050-2007 is " Code for design of industrial recirculating cooling water treatment ".
Embodiment 2
Certain Coking Plant Wastewater is handled using the integrated process flow in the method for the present invention attached drawing 2, water quality indicator is such as
Under:
| Serial number | Project | Unit | Influent quality |
| 1 | CODCr | mg/L | ≤3500 |
| 2 | NH3-N | mg/L | ≤140 |
| 3 | Chloride ion | mg/L | ≤500 |
| 4 | Turbidity | NTU | ≤240 |
| 5 | Total hardness is (with CaCO3Meter) | mg/L | ≤280 |
| 6 | Total dissolved solid (TDS) | mg/L | ≤3500 |
| 7 | pH | - | 6~9 |
The system the following steps are included:
A, pretreating process
Waste water sequentially enters oil separator, flotation tank, crystallization fluorine removal reactor first and is pre-processed.By pretreatment, go
Except the oils of useless water part, solid suspension, fluorine ion and organic matter etc..
Pretreatment water outlet: turbidity≤30NTU, COD≤2400mg/L, water outlet flow into comprehensive wastewater conditioning tank and carry out water quality water
The adjusting of amount.
B, biochemical processing process
Biochemical processing process unit uses anaerobic- anoxic- oxic (A2O) technique carries out COD to waste water and nitrogen, phosphorus is gone
It removes.
By biochemical treatment unit, COD≤180mg/L of waste water, ammonia nitrogen≤3mg/L.
C, depth pretreating process
Biochemistry pool water outlet is promoted through pump, after adding ferrous sulfate and hydrogen peroxide, into improvement Fenton oxidation reactor, is occurred
Oxidation reaction removes most hardly degraded organic substance.After improveing Fenton catalytic oxidation, COD≤60mg/L.Water outlet
NaOH is added through pipe-line mixer and adjusts pH to 7.5 or so, and into manganese sand filter, the water outlet of manganese sand filter is lifted into more Jie through pump
Mass filter fine filtering.
After manganese sand and multimedium double-filtration, turbidity≤1.0NTU in waste water, total iron≤0.3mg/L.
D, advanced treatment process
Multimedium water outlet successively carries out advanced treating by ultrafiltration apparatus, resin softening plant and reverse osmosis unit.Ultrafiltration
Film uses external pressing type hollow fibrous membrane element, intake pressure 0.2MPa, ultra-filtration water turbidity≤0.1NTU, value≤3 SDI.Ultrafiltration
Water outlet enters resin softening plant, which uses sodium form cation exchange resin, and the calcium and magnesium ion removed in waste water reduces water
Hardness go out the water hardness≤5mg/L to guarantee the normal operation of reverse osmosis membrane.Reverse osmosis unit uses anti-pollution reverse-osmosis
Film, operating pressure 1.5MPa of intaking, the rate of recovery 75%.
Reverse osmosis unit effluent quality is as follows: COD≤15mg/L, TDS≤100mg/L, chloride ion≤30mg/L, hardness≤
0.5mg/L, ammonia nitrogen≤0.2mg/L, turbidity≤0.1NTU, pH value 7.0~7.5, water quality indicator meet " at industrial circulating cooling water
Manage design specification " requirement can reuse.
E, concentrated water treatment process
The concentrated water water quality indicator of reverse osmosis unit are as follows: COD≤210mg/L, conductivity≤15000 μ S/cm, chloride ion≤
1820mg/L, hardness≤25mg/L, turbidity≤0.1NTU.
The concentrated water of reverse osmosis unit is promoted to targeting catalyst oxidation reactor through pump, strengthens the difficult drop being concentrated in removal concentrated water
Organic matter is solved, COD≤58mg/L, turbidity≤7NTU are discharged.It flows into fiber ball filter from top to bottom later, carries out deep layer and cut
Dirt, delivery turbidity value≤0.5NTU.Effluent quality through targeting catalytic oxidation and fiber ball filter reaches concentrated type electricity
The water inlet index request of electrodialysis apparatus.The concentrated type electrodialysis plant used is vertical structure, intake pressure≤0.4MPa, concentrated water
After concentrated type electrodialysis process, the rate of recovery reaches 79%, and salt rejection rate 70%, concentrated water conductivity≤60000 μ S/cm produces water power
Conductance≤4500 μ S/cm.The production water of concentrated type electrodialysis plant is back to feed water by reverse osmosis mouth and further recycles, through reverse osmosis membrane
Product water reuse is used as after desalination.The concentrated water of the electrodialysis plant enters nanofiltration device, using nanofiltration membrane to the selectivity of ion
Retention so that chloride ion and sulfate ion separate in waste water, the film to the rejection of sulfate ion reach 98% with
On.Nanofiltration containing chloride ion produces water and enters the first bipolar membrane electrodialysis device, and the salting liquid based on NaCl is converted into salt
Acid and sodium hydroxide solution, conversion ratio reach 95%；And the nanofiltration concentrated water containing sulfate ion enters the second Bipolar Membrane electric osmose
Analysis apparatus, will be with Na2SO4Sulfuric acid and sodium hydroxide solution, conversion ratio 93% are converted into for main salting liquid.Bipolar membrane electrodialysis
The hydrochloric acid that device generates can be used for the chemical cleaning of the devices such as resin regeneration and ultrafiltration, electrodialysis；The sulfuric acid of generation can be used for
The adjusting of system pH；The sodium hydroxide solution of generation can be used for resin regeneration, the adjusting of system pH and ultrafiltration, electrodialysis plant
Chemical cleaning.
Extra hydrochloric acid solution, sulfuric acid solution and sodium hydroxide solution is used for the not high soda acid purposes of quality requirements.
Dross, the sludge generated in the system forms mud cake after being dehydrated, and can be used as light ceramic, eco-cement, brick etc.
The raw material of building materials.
Effluent quality index reaches the requirement of " Code for design of industrial recirculating cooling water treatment ", and specific data are as follows:
Note: GB 50050-2007 is " Code for design of industrial recirculating cooling water treatment ".
Embodiment 3:
Certain coal gas wastewater is handled using the integrated process flow in the method for the present invention attached drawing 2.Water quality indicator is such as
Under:
| Serial number | Project | Unit | Influent quality |
| 1 | CODCr | mg/L | ≤5200 |
| 2 | NH3-N | mg/L | ≤175 |
| 3 | Chloride ion | mg/L | ≤280 |
| 4 | Turbidity | NTU | ≤190 |
| 5 | Total hardness is (with CaCO3Meter) | mg/L | ≤330 |
| 6 | Total dissolved solid (TDS) | mg/L | ≤3000 |
| 7 | pH | - | 8.0~9.0 |
The system the following steps are included:
A, pretreating process
Waste water sequentially enters oil separator, flotation tank, crystallization fluorine removal reactor first and is pre-processed.By pretreatment, go
Except the oils of useless water part, solid suspension, fluorine ion and organic matter etc..
Pretreatment water outlet: turbidity≤25NTU, COD≤3000mg/L, water outlet flow into comprehensive wastewater conditioning tank and carry out water quality water
The adjusting of amount.
B, biochemical processing process
Biochemical processing process unit uses anaerobic- anoxic- oxic (A2O) technique carries out COD to waste water and nitrogen, phosphorus is gone
It removes.
Biochemical treatment water outlet: COD≤200mg/L, ammonia nitrogen≤5mg/L.
C, depth pretreating process
Biochemistry pool water outlet is promoted through pump, into targeting catalyst oxidation reactor.Targeting catalytic oxidation is in reactor
Middle filling needle is passed through ozone to the targeting catalyst of coal gas wastewater water quality characteristics, is made by the inducing action of catalyst
Ozone accelerated decomposition generates the hydroxyl radical free radical of strong oxidizing property, and the characteristic contamination in waste water is thoroughly decomposed, and water outlet COD≤
52mg/L sequentially enters manganese sand filter and more medium filter.
After manganese sand and multimedium double-filtration, turbidity≤1.0NTU in waste water, total iron≤0.2mg/L.
D, advanced treatment process
Multimedium water outlet successively carries out advanced treating by ultrafiltration apparatus, resin softening plant and reverse osmosis unit.Ultrafiltration
Film uses external pressing type hollow fibrous membrane element, intake pressure 0.2MPa, ultra-filtration water turbidity≤0.1NTU, value≤3 SDI.Ultrafiltration
Water outlet enter resin softening plant, the device use Hydrogen weak-acid cation-exchange resin, remove waste water in calcium, magnesium from
Son reduces the hardness of water, to guarantee the normal operation of reverse osmosis membrane, goes out the water hardness≤3mg/L.Reverse osmosis unit uses anti-pollution
Reverse osmosis membrane is contaminated, operating pressure 1.4MPa of intaking, the rate of recovery 75%.
The effluent quality of reverse osmosis unit is as follows: COD≤20mg/L, TDS≤85mg/L, chloride ion≤20mg/L, hardness
≤ 0.3mg/L, ammonia nitrogen≤0.5mg/L, turbidity≤0.1NTU, pH value 7.5~8.0, water quality indicator meet " industrial circulating cooling water
Handle design specification " requirement can reuse.
E, concentrated water treatment process
The concentrated water water quality indicator of reverse osmosis unit are as follows: COD≤178mg/L, conductivity≤16750 μ S/cm, chloride ion≤
1340mg/L, hardness≤11mg/L, turbidity≤0.1NTU.
The concentrated water of reverse osmosis unit is promoted to targeting catalyst oxidation reactor through pump, strengthens the difficult drop being concentrated in removal concentrated water
Organic matter is solved, COD≤44mg/L, turbidity≤5NTU are discharged.It flows into fiber ball filter from top to bottom later and carries out deep layer section dirt,
Delivery turbidity value≤0.6NTU.It is electrodialytic that effluent quality through targeting catalytic oxidation and fibre-ball filtration reaches concentrated type
Water inlet index request.The concentrated type electrodialysis used is vertical structure, intake pressure 0.4MPa, the concentrated type electrodialysis of concentrated water
Afterwards, the rate of recovery 85%, salt rejection rate reach 73%, and concentrated water conductivity≤88000 μ S/cm produces water conductivity≤4500 μ S/cm,
Product water reuse is used as after reverse osmosis membrane is desalinated.The concentrated water of the electrodialysis plant enters nanofiltration device, using nanofiltration membrane to from
The selectivity of son retains so that chloride ion and sulfate ion separate in waste water, which reaches the rejection of sulfate ion
To 98% or more.Nanofiltration containing chloride ion produces water and enters the first bipolar membrane electrodialysis device, by the salting liquid based on NaCl
Convert hydrochloric acid and sodium hydroxide solution, conversion ratio 95%；And the nanofiltration concentrated water containing sulfate ion is bipolar into second
Membrane electrodialysis device, will be with Na2SO4Based on salting liquid be converted into sulfuric acid and sodium hydroxide solution, conversion ratio 93%.It is bipolar
The hydrochloric acid that membrane electrodialysis device generates can be used for the chemical cleaning of the devices such as resin regeneration and ultrafiltration, electrodialysis；The sulphur of generation
Acid can be used for the adjusting of system pH；The sodium hydroxide of generation can be used for resin regeneration, the adjusting of system pH and ultrafiltration, electrodialysis
The chemical cleaning of device.
Extra hydrochloric acid solution, sulfuric acid solution and sodium hydroxide solution is used for the not high soda acid purposes of quality requirements.
Dross, the sludge generated in the system forms mud cake after being dehydrated, and can be used as light ceramic, eco-cement, brick etc.
The raw material of building materials.
The requirement for reaching " Code for design of industrial recirculating cooling water treatment " by advanced treating effluent quality index, can return
With specific data are as follows:
Note: GB 50050-2007 is " Code for design of industrial recirculating cooling water treatment ".
The present invention is described in detail above by specific and preferred embodiment, but those skilled in the art should be bright
White, the present invention is not limit to that embodiments describe above, all within the spirits and principles of the present invention, made any modification,
Equivalent replacement etc., should all be included in the protection scope of the present invention.
Claims (6)
1. a kind of resource utilization of high-concentration hardly-degradable salt-containing organic wastewater utilizes processing system characterized by comprising
Crystallization fluorine removal reactor: being wherein added and defluorinating agent and stir, for by high-concentration hardly-degradable saliferous organic waste to be processed
Fluorine ion in water is removed in the form of sediment, to reduce the fouling risk that subsequent membranous system is generated by calcirm-fluoride；
Comprehensive wastewater conditioning tank: water quality, the adjusting crystallization fluorine removal for the uniformly water outlet of the crystallization fluorine removal reactor are anti-
Answer the water of the water outlet of device；
Biochemical treatment system: for the water outlet of the comprehensive wastewater conditioning tank, realizing the degradation of COD under the action of microorganism,
The synchronous removal for realizing nitrogen and phosphorus；
Advanced oxidation unit: for the water outlet of the biochemical treatment system, removing difficult to degrade in the biochemical treatment system has
Machine object reduces the risk that subsequent desalination system generates organic pollution；
Include improvement Fenton oxidation reaction system and/or targeting catalytic oxidation system in the advanced oxidation unit；
The improvement Fenton oxidation reaction system adds ferrous sulfate and hydrogen peroxide under conditions of not acid adding, has pollutant
Degradation capability, also reduction reagent consumption amount and sludge yield；
Filling needle is to the catalyst of different quality feature in the described targeting catalytic oxidation system, and is passed through ozone, passes through
The inducing action of catalyst makes the hydroxyl radical free radical of ozone accelerated decomposition generation strong oxidizing property, by the characteristic contamination in waste water
Thoroughly decompose；
Filter element: for the water outlet of the advanced oxidation unit to be filtered, delivery turbidity is reduced；
The filter element includes the combination of manganese sand filter or more medium filter or both；
By the iron ion and manganese ion in aeration removal waste water in the manganese sand filter, and by the manganese sand filter
Manganese sand filtering material primary filtration removes partial suspended thing；
The more medium filter carries out fine filtering, and quartz sand and ANTHRACITE FILTER MEDIA are housed in the more medium filter, gone
Except fine suspension and reduce delivery turbidity；
The partial size of manganese sand filtering material in the manganese sand filter is 1-2mm；
The partial size of the quartz sand and ANTHRACITE FILTER MEDIA that are equipped in the more medium filter is 0.8-1.2mm；
Ultrafiltration apparatus: for further removing the suspended matter in the water outlet of the filter element, colloid, microorganism；
Resin softening plant: for the water outlet of the ultrafiltration apparatus, removing calcium ion and magnesium ion, reduce subsequent desalination system without
The risk of machine salt fouling；The calcium chloride and magnesium chloride contained in the acid-basic regenerated waste liquids in water of the resin softening plant, is back to institute
Crystallization fluorine removal reactor is stated to use as defluorinating agent；
Reverse osmosis unit: it for the water outlet of the resin softening plant and the production water of concentrated type electrodialysis plant, reduces therein
Inorganic salt concentration, while removing remaining organic matter；The production water of the reverse osmosis unit is as product water reuse；
Concentrated type electrodialysis plant: for the concentrated water of the reverse osmosis unit to be further concentrated；The concentrated type electrodialysis dress
The production water set is back to the reverse osmosis unit and further recycles；
Nanofiltration device: for separating sulfate ion in the concentrated water of the concentrated type electrodialysis plant and chloride ion；
First bipolar membrane electrodialysis device: the nanofiltration for containing chloride ion for the nanofiltration device produces water, will be based on NaCl
Salting liquid is converted to hydrochloric acid solution and sodium hydroxide solution；
Second bipolar membrane electrodialysis device: containing the nanofiltration concentrated water of sulfate ion for the nanofiltration device, will be with Na2SO4For
Main salting liquid is converted to sulfuric acid solution and sodium hydroxide solution；
It further include that targeting catalyst oxidation reactor and fiber ball filter, the concentrated water of the reverse osmosis unit initially enter the target
To catalyst oxidation reactor, the hardly degraded organic substance being concentrated in concentrated water is removed；Fiber ball filter is entered back into, deep layer is carried out and cuts
It is dirty；Then the concentrated type electrodialysis plant is entered back into further to be concentrated；
It further include the cartridge filter required for meeting the water inlet of reverse osmosis unit, the water outlet of the resin softening plant is passed through
After the cartridge filter, the reverse osmosis unit is entered back into；
Further include self-cleaning filter, after the water inlet of the ultrafiltration apparatus will first pass through the self-cleaning filter, enters back into institute
State ultrafiltration apparatus.
2. the resource utilization of high-concentration hardly-degradable salt-containing organic wastewater according to claim 1 utilizes processing system,
Be characterized in that: further including oil separator and flotation tank, high-concentration hardly-degradable salt-containing organic wastewater to be processed initially enter it is described every
After oil sump and the flotation tank, the crystallization fluorine removal reactor is entered back into.
3. the resource utilization of high-concentration hardly-degradable salt-containing organic wastewater according to claim 2 utilizes processing system,
It is characterized in that: further including sludge-tank and sludge dewatering equipment, the flotation tank, the crystallization fluorine removal reactor and the biochemical treatment
Sediment in system enters the sludge-tank, and then after sludge dewatering equipment dehydration, sludge is transported.
4. the resource utilization of high-concentration hardly-degradable salt-containing organic wastewater according to claim 1 utilizes processing system,
It is characterized in that: further including manganese sand discharge bay, the water outlet of the manganese sand filter first passes through the manganese sand discharge bay and then enters back into down
One device；
It further include multimedium discharge bay, the water outlet of the more medium filter first passes through the multimedium discharge bay and then enters back into
Next device；
It further include bio-chemical effluent pond, the water outlet of the biochemical treatment system first passes through the bio-chemical effluent pond and then enters back into next
A device；
It further include ultra-filtration water pond, the water outlet of the ultrafiltration apparatus first passes through the ultra-filtration water pond and then enters back into next dress
It sets；
It further include softening discharge bay, the water outlet of the resin softening plant first passes through the softening discharge bay and then enters back into next
A device；
It further include reverse osmosis water outlet pond, the water outlet of the reverse osmosis unit first passes through the reverse osmosis water outlet pond and then enters back into down
One device.
5. the resource utilization of high-concentration hardly-degradable salt-containing organic wastewater according to claim 1 utilizes processing system,
It is characterized in that: adding the defluorinating agent in the crystallization fluorine removal reactor, and be sufficiently stirred so that the high-concentration hardly-degradable
Salt-containing organic wastewater is centrifuged after forming crystal, removes fluorine ion therein with solid forms；The defluorinating agent is chlorine
Change one or both of calcium or magnesium chloride.
6. the resource utilization of high-concentration hardly-degradable salt-containing organic wastewater according to claim 1 utilizes processing system,
Be characterized in that: the resin softening plant uses sodium form cation exchange resin, Hydrogen weak-acid cation-exchange resin or chela
One of resin form；
The nanofiltration device is retained using selectivity of the nanofiltration membrane to ion, and sulfate ion and chloride ion are separated；
Regeneration of the hydrochloric acid solution generated in first bipolar membrane electrodialysis device for resin in the resin softening plant,
And for the chemical cleaning including the ultrafiltration apparatus, concentrated type electrodialysis plant；
The sulfuric acid solution generated in second bipolar membrane electrodialysis device is used for the high-concentration hardly-degradable salt-containing organic wastewater
Resource utilization using the system pH in treatment process adjusting；
The sodium hydroxide solution generated in first bipolar membrane electrodialysis device and second bipolar membrane electrodialysis device is used
The regeneration of resin and the resource utilization for the high-concentration hardly-degradable salt-containing organic wastewater in the resin softening plant
Using the adjusting of the system pH in treatment process, and for including the ultrafiltration apparatus, concentrated type electrodialysis plant
Chemical cleaning.
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