CN202865020U - Chlor-alkali industrial wastewater zero discharge system - Google Patents
Chlor-alkali industrial wastewater zero discharge system Download PDFInfo
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- CN202865020U CN202865020U CN 201220507198 CN201220507198U CN202865020U CN 202865020 U CN202865020 U CN 202865020U CN 201220507198 CN201220507198 CN 201220507198 CN 201220507198 U CN201220507198 U CN 201220507198U CN 202865020 U CN202865020 U CN 202865020U
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Abstract
The utility model discloses a chlor-alkali industrial wastewater zero discharge system which comprises a sodium hypochlorite wastewater treatment system, a centrifugal mother liquid treatment system, a comprehensive wastewater treatment system, a domestic sewage treatment system and a circulating water system. After treating well water through a water desalination device, produced desalted water is conveyed to a caustic soda device, a polyvinyl chloride (PVC) polymerization device for production use; one part of concentrated salt water generated by the water desalination device is applied to an acetylene generator, and one part of concentrated salt water is fed into a light salt water groove and returned to a bittern well to collect bittern; a production water station is mainly applicable to an acetylene cleaning device, a PVC polymerization generation device, the caustic soda device and an acetylene section alkali washing tower; the sodium hypochlorite wastewater from the acetylene cleaning device is treated by the sodium hypochlorite wastewater treatment system and is applied to the bittern well to collect the bittern after reaching the standard; the centrifugal mother liquid from the PVC polymerization generation device is treated by the centrifugal mother liquid treatment system and is applied to the circulating water system after reaching the standard; and the production wastewater from the PVC polymerization generation device and the production wastewater from the caustic soda device are treated by the comprehensive wastewater treatment system and are applied to the bittern well to collect the bittern from light salt water after reaching the standard.
Description
Technical field
The utility model belongs to discharging and the reuse problem of chlor-alkali industrial waste water, is applied to the processing of chlor-alkali industrial waste water, finally realizes waste water zero emission.
Background technology
Chlorine industry is one of the most basic chemical industry, the chlorine-alkali products such as polyvinyl chloride (PVC) RESINS, caustic soda, hydrochloric acid, liquid chlorine all are national economy and the requisite material of people's lives, in national economy and national defense construction, occupy critical role, but the chlor-alkali industry environmental pollution also is larger simultaneously.Along with the enhancing of people to environmental protection consciousness, pollution of being caused in take chlorine industry as the chemical process on basis and products thereof is more and more paid attention to the impact that environment causes.Therefore, give full play to chlorine industry and take chlorine industry as the basis the effect of Chemical Manufacture in the national economic development in, should reduce it to the disadvantageous effect of environment as far as possible.
In chlorine industry, PVC polymerization generating apparatus can produce a large amount of centrifuge mother liquors, and the acetylene cleaning device can produce a large amount of inferior sodium waste water, and soda equipment and other production workshop sections all can produce a large amount of waste water.At present in the chlorine industry, these waste water seldom are recycled utilization, all are through directly discharging after the simple process in a large number, contaminate environment not only, and wasted resource, be unfavorable for energy-saving and emission-reduction.
In chlorine industry, the rainwater of plant area and domestic water all are direct dischargings, are not utilized, and also are unfavorable for energy-saving and emission-reduction.
The utility model content
The purpose of this utility model is to overcome above-mentioned deficiency a kind of chlor-alkali industrial waste water Zero discharging system is provided, and realized that rain is dirty, removed contamination, dirty shunting, the sub-prime discharging, sub-prime is processed, separate-recycling.
For achieving the above object, the utility model is by the following technical solutions:
A kind of chlor-alkali industrial waste water Zero discharging system, comprise time sodium Waste Water Treatment, the centrifuge mother liquor treatment system, comprehensive wastewater treatment system, domestic sewage processing system and circulating water system, well water is transported to soda equipment with the de-salted water of producing after processing by the de-salted water device, the PVC poly-unit is for production and application, the strong brine part that the de-salted water device produces is used for carbide-feed generator, a part is sent into the light salt brine groove and is returned sub-salt well and adopt halogen, the water of productive use station owner will supply the acetylene cleaning device, PVC polymerization generating apparatus, soda equipment and acetylene section soda-wash tower use, after time sodium Waste Water Treatment processing is up to standard, be back to sub-salt well from acetylene cleaning device inferior sodium waste water out and be used for adopting halogen, after the processing of centrifuge mother liquor treatment system is up to standard, be back to circulating water system from PVC polymerization generating apparatus centrifuge mother liquor out, from PVC polymerization generating apparatus out factory effluent and process through comprehensive wastewater treatment system from soda equipment factory effluent out and to be back to sub-salt well after up to standard and to be used for light salt brine and to adopt halogen, water in water circulating system with water is back to use carbide-feed generator, enter the centrifuge mother liquor processing unit after domestic water is processed by the sanitary wastewater treatment system and carry out advanced treatment, be back to circulating water system after qualified.
Above-mentioned chlor-alkali industrial waste water Zero discharging system is characterized in that: also comprise slag stock tank treatment system, acetylene section soda-wash tower mercury-containing waste water out is used for cement plant and is made into cement after slag stock tank treatment system is processed.
Above-mentioned chlor-alkali industrial waste water Zero discharging system, described centrifuge mother liquor treatment system comprises the cooling tower that connects by pipeline successively, the Two-Stage Biochemical reaction tank, settling tank, intermediate pool, strainer and reuse tank, also comprise the backwashing wastewater pond, sludge sump and sludge dewatering system, centrifuge mother liquor passes through cooling tower successively, the Two-Stage Biochemical reaction tank, settling tank, intermediate pool and strainer, processing water after at last up to standard enters reuse tank, by pump to squeezing into the circulating water system reuse, mud in the settling tank after the precipitation enters sludge sump, mud in the sludge sump pumps into sludge dewatering system, through the outward transport of the mud cake after the dehydration, use the Two-Stage Biochemical reaction tank at sludge dewatering system processing water out by back of pipeline, the slurry that strainer filters enters the backwashing wastewater pond, and the backwashing wastewater pond pumps into Two-Stage Biochemical reaction tank recycling processing by pump with the water in the backwashing wastewater pond.
Above-mentioned chlor-alkali industrial waste water Zero discharging system adds simultaneously air blast of nutritive salt in the described Two-Stage Biochemical reaction tank, enter settling tank behind biochemical reaction, and filters and be delivered to circulating water system when making water quality reach the recirculated water reuse standard.
Above-mentioned chlor-alkali industrial waste water Zero discharging system, described comprehensive wastewater treatment system comprises the equalizing tank that connects successively, neutralization tank, coagulation basin, settling tank, intermediate pool, valveless water filter device and reuse tank, also comprise sludge sump, comprehensive wastewater flows into equalizing tank through grille well, equalizing tank pumps into neutralization tank, with the pH value in HCl and the NaOH adjusting neutralization tank, when the pH value is discharged in the coagulation basin during for 6-9, enter successively again intermediate pool and valveless water filter device, processing water after the filtration enters reuse tank, reuse tank is connected to the sub-salt well reuse by pipeline, the mud of settling tank precipitation pumps into comprehensive sludge sump, air blast pumps into mother liquor unit sludge dewatering system simultaneously in the sludge sump, and the supernatant liquor in the sludge sump turns back to equalizing tank, and the filtration slurry after the valveless water filter device is processed turns back to the equalizing tank circular treatment.
Above-mentioned chlor-alkali industrial waste water Zero discharging system is communicated with in intermediate pool and middle the pipe by leap of reuse tank.
Above-mentioned chlor-alkali industrial waste water Zero discharging system, described sodium Waste Water Treatment is by the gas stripping column that connects by pipeline successively, cooling tower, the first pH regulator pond, oxidation pond, the second pH regulator pond, the dephosphorization pond, settling tank, sludge sump, comprehensive sludge sump and sludge treating system, also comprise intermediate pool, hay tank and clean water basin, inferior sodium waste water enters cooling tower behind gas stripping column, cooling tower inferior sodium waste water out enters the first pH regulator pond, regulate pH value in the first pH regulator pond with HCl and NaOH, when the pH value is discharged in the oxidation pond during for 6-9, adding oxygenant in the oxidation pond carries out entering the second pH regulator pond after the oxidation, with the pH value in HCl and the NaOH adjusting neutralization tank, when the pH value enters the dephosphorization pond during for 6-9, be discharged into settling tank after adding the dephosphorization agent reaction, supernatant liquid enters into intermediate pool, with the pH value in HCl and the NaOH adjusting intermediate pool, when pH value 6-7, be drained into hay tank, filtered clear water is back to use sub-salt well after entering into clean water basin, backwashing wastewater after hay tank filters turns back to a pH value equalizing tank and carries out circular treatment, the slip of settling tank lower floor pumps into sludge sump, the supernatant liquid of sludge sump turns back to a pH value equalizing tank and carries out circular treatment, and the material of sludge sump lower floor enters into comprehensive sludge sump and carries out sludge treatment.
Above-mentioned chlor-alkali industrial waste water Zero discharging system is all sent into pressurized air when a pH value equalizing tank, the 2nd pH value equalizing tank and intermediate pool adjust pH.
Above-mentioned chlor-alkali industrial waste water Zero discharging system, described sanitary wastewater treatment system comprises grille well, sanitary wastewater flows into settling pit after by grille well, lower floor's mud of settling pit pumps into comprehensive sludge sump, the supernatant liquid of settling pit enters equalizing tank and integration apparatus, enter settling tank after again processing, the supernatant liquid of settling tank enters the centrifuge mother liquor processing unit, and the lower floor of settling tank turns back to the settling pit circular treatment.
Above-mentioned chlor-alkali industrial waste water Zero discharging system, described de-salted water device comprise five processing units such as pre-treatment, reverse osmosis, precision processing, phlegma recovery, strong brine recovery.
Adopt technique scheme, the utility model has following advantage: at present, realization trade effluent " zero release " technology is not yet arranged in the chlorine industry, this utility model takes the lead in having realized at chlor-alkali enterprises " rain is dirty, remove contamination, dirty shunting ", be that sub-prime discharging, sub-prime are processed, separate-recycling, so that pointed to the processing of waste water, the difference according to water quality after processing can be back to different water operations, can farthest realize the recycling to waste water; The dirty shunting of rain is so that rainwater enters separately natural water, and sewage enters waste disposal plant and carries out individual curing, and the design and construction expense is loaded, reduced in the processing that has reduced sewage treatment structure.The same industry belongs to innovative technology at home.Centrifuge mother liquor is processed and is back to light salt brine after rear reuse circulating water system up to standard, the clorox wastewater treatment and adopts and be back to light salt brine after halogen, comprehensive wastewater are processed and return well and adopt halogen, has creatively carried out reuse according to the difference of production equipment water water quality especially in the same industry.Mercury-containing waste water is sent to the slag stock tank through outer piping lane, and slag is starched next making cement, thoroughly eliminates the mercury evil.The sanitary sewage of processing after qualified enters the mother liquor pond, and the sewage of whole system, the equal fully recovering of waste water finally reach " zero release " effect.This utility model " zero release " scheme for the rationally collection of all kinds of sewage of chlor-alkali enterprises, optimal treatment, have and select reuse, " zero " discharging and research, all kinds of sewage discharges of present domestic chemical industry for making chlorine and alkali are disorderly, intractability is large, processing costs is high to solving, the sewage after the processing is difficult for the problems such as up to standard.Make waste water accomplish really that from producing to discharge sub-prime is collected, sub-prime is processed, separate-recycling, thereby reach the effect of rational utilization of water resources, energy-saving and cost-reducing, protection of the environment, make trade effluent really can reach zero release.All types of industries discharge of wastewater pipeline is respectively composite wastewater, sanitary sewage, rainwater (peace and quiet) water discharge line, the pipelines such as water of condensation, the dense water of de-salted water, centrifugal mother liquor waste water, inferior sodium waste water, soda-wash tower waste water, centrifuge mother liquor reuse water, comprehensive wastewater.The reuse water pipeline has Wastewater Form Circulating Cooling Water, the dense water of de-salted water, centrifuge mother liquor to process qualified water, useless time sodium is processed the reuse water pipelines such as qualified water, comprehensive treating process qualified water, mercury-containing waste water, has reached and all has been sent to reuse point condition.
Make a concrete analysis of as follows:
(1) soda-wash tower mercury-containing waste water: the stock tank that removes slag after the processing, S2-reaction in Hg2+ and the slag slurry generates the HgS precipitation, comes along cement processed with the slag slurry, thoroughly eliminates the mercury evil, and environment protection significance is huge.
(2) centrifuge mother liquor is processed and to be back to circulating water system after qualified: the centrifuge mother liquor device designing treatment water yield 65 m3/h, normal 40m3/h, COD350mg/l, ammonia nitrogen 13.1mg/l, water outlet COD is that 40mg/l, ammonia nitrogen are 5mg/l after processing, be back to circulating water system water yield 60m3/h, move per year 8000h and calculate;
A, year reduce the COD quantity discharged: centrifuge mother liquor COD content 310 mg/l that average.
310mg/l * 40 * 103l/h * 8000h=128.8 * 109mg=99.2 ton;
B, expenses of environmental protection: collect 1.0 yuan of calculating of effluent charge by waste water per ton, can reduce row every year
Dirty expense: 40m3/h * 8000h * 1.0 yuan/tons=320,000 yuan;
C, water saving expense: but be back to circulating water system saving water resource in the year after next 320000 m3,
Expense is calculated by 1.8 yuan/m3, year saves working cost: ten thousand yuan of 320,000 m3 * 1.8 yuan/m3=57.6.
D, total are reduced expenses: ten thousand yuan/year of 32+57.6=89.6.
(3) the useless time qualified rear reuse light salt brine groove of sodium water treatment returns well and adopts halogen:
Useless time the sodium water treatment device designs 25 m3/h, and normal 15 m3/h by year operation 8000h at full capacity, adopt halogen with 1.8 yuan/m3 of water price lattice, and 1.0 yuan of ton water effluent charge then have:
A, year minimizing COD quantity discharged: 100mg/l * 15 * 103l/h * 8000h=12 * 109mg=12 ton;
B, expenses of environmental protection: 15m3/h * 8000h * 1.0 yuan/ton=120,000 yuan
C, year save working cost: 15m3/h * 8000h * 1.8 yuan/ten thousand yuan of m3=21.6 (during normal line balancing).
D, total are reduced expenses: ten thousand yuan/year of 12+21.6=33.6
(4) the NF concentrated water reuse acetylene of de-salted water generation occurs and returns well and adopt halogen
Produce the dense water of the dense water side of reverse osmosis membrane generating portion in the process at pure water, saltiness is large, if directly draining, this part waste water causes the wasting of resources, according to the water quality after processing and in conjunction with my company's actual process situation, water after this partially disposed is delivered to the light salt brine system to be returned sub-salt well and adopts halogen or be sent to configuration time sodium and acetylene occurs, the water yield is 53m3/h approximately, device is by year is moved 8000h at full capacity, 1.8 yuan/m3 of water price lattice, year recyclable water resources 42.4 ten thousand m3 then, reduce expenses 76.3 ten thousand yuan, the energy-saving and emission-reduction meaning is huge.
(5) Reuse of Wastewater Form Circulating Cooling Water acetylene occurs
Normal blowdown 74 m3/h can be down to blowdown flow rate about 40m3/h after the centrifugal mother liquor waste water reuse.And direct reuse occurs in acetylene, but water saving 320,000 m3, if 1.8 yuan/m3 of water price lattice.Then reduce expenses and be ten thousand yuan/year of 40 * 8000 * 1.8=57.6
(6) recovery of water of condensation and heat reuse
The recycling condensing water meaning is huge, and through preresearch estimates, the economical effectiveness that obtains is as follows:
A, be 42.4m3/h by the normal yield of phlegma, then reduce discharging altogether phlegma the whole year
42.4m3/h * 8000h=33.92 ten thousand m3 save former water 33.92 ten thousand m3,1 m3 phlegma is 6.8 yuan by the pure water calculation of price, and the former water price lattice of 1 m3 are 1.8 yuan; Year saving expense then: 275.2 ten thousand yuan in the unit of 33.92 ten thousand m3 * (6.8+1.8)/m3 ≈.
B, phlegma are used for former water is carried out heat exchange, and can reduce the steam usage quantity every year, and specific heat of water is 4.2KJ/Kg90 ℃, and condensate temperature is down to 25 ℃ after the heat exchange, then has:
Year can be utilized latent heat (90 ℃-25 ℃) * 4200J/(Kg. ℃) * 1000Kg/ m3 * 40m3/h * 8000h=0.87 * 10
11KJ;
But 1 year steam saving: 0.87 * 10
1141271 tons of KJ ÷ 2108KJ/Kg ≈;
But every year the steam saving expense: 6,190,000 yuan of 41271 tons * 150 yuan/tons ≈.
Then annual expectation produces economic benefit: 894.2 ten thousand yuan.
(7) comprehensive wastewater is processed qualified rear reuse and is adopted halogen:
Comprehensive wastewater designing treatment amount is 80 m3/h, normal 45 m3/h, we also are back to the light salt brine system with this part water and return the light salt brine groove and adopt halogen, press at full capacity year operation 8000h of device, adopt halogen with 1.8 yuan/m3 of water price lattice, 1 year recoverable water resources 45m3/h * 80,00h,=36 ten thousand m3 then save ten thousand yuan of working cost 36 m3 * 1.8 yuan/m3=64.8.
Save working cost: ten thousand yuan of 360,000 m3 * 1.8 yuan/m3=64.8;
If below carry out fully, water energy complete equipilibrium can be saved as follows: water 218.4 ten thousand m
3/ year; 41271 tons of steam.Year reduces expenses approximately altogether: ten thousand yuan of 89.6+33.6+76.3+57.6+894.2+64.8=1216.1
Description of drawings
Fig. 1 is structural representation of the present utility model.
Fig. 2 is the utility model centrifuge mother liquor treatment system structural representation.
Fig. 3 is the utility model time sodium Waste Water Treatment structural representation.
Fig. 4 is the utility model comprehensive wastewater treatment system structural representation.
Fig. 5 is the utility model desalting plant structural representation.
Fig. 6 is the utility model sanitary wastewater treatment system structural representation.
Embodiment
Such as Fig. 1-a kind of chlor-alkali industrial waste water Zero discharging system shown in Figure 6, comprise time sodium Waste Water Treatment, the centrifuge mother liquor treatment system, comprehensive wastewater treatment system, domestic sewage processing system and circulating water system, well water is transported to soda equipment with the de-salted water of producing after processing by the de-salted water device, the PVC poly-unit is for production and application, the strong brine part that the de-salted water device produces is used for carbide-feed generator, a part is sent into the light salt brine groove and is returned sub-salt well and adopt halogen, the water of productive use station owner will supply the acetylene cleaning device, PVC polymerization generating apparatus, soda equipment and acetylene section soda-wash tower use, after time sodium Waste Water Treatment processing is up to standard, be back to sub-salt well from acetylene cleaning device inferior sodium waste water out and be used for adopting halogen, after the processing of centrifuge mother liquor treatment system is up to standard, be back to circulating water system from PVC polymerization generating apparatus centrifuge mother liquor out, soda equipment comprehensive wastewater out is back to sub-salt well and is used for adopting halogen after the comprehensive wastewater treatment system processing is up to standard, water in water circulating system with water is back to use carbide-feed generator, enter the centrifuge mother liquor processing unit after sanitary sewage is processed by domestic sewage processing system and carry out advanced treatment, and be back to circulating water system.
Also comprise acetylene section soda-wash tower, acetylene section soda-wash tower mercury-containing waste water out is used for cement plant and is made into cement after the slag stock tank is processed.
The soda-wash tower mercury-containing waste water removes the carbide slag stock tank after processing,
Wastewater source and index:
Mercury-containing waste water is mainly derived from soda-wash tower, and index is as follows:
Process choice
Mercury-containing waste water is the difficult problem of industry wastewater treatment always, and we find a good method, is exactly by after increasing some equipment, is sent to my company's slag stock tank through outer piping lane, and the slag stock tank is making cement next, thoroughly eliminates the mercury evil.
Reaction equation: Hg2-+S2--HgS ↓.
Above-mentioned chlor-alkali industrial waste water Zero discharging system, described centrifuge mother liquor treatment system comprises cooling tower, Two-Stage Biochemical reaction tank, settling tank, intermediate pool, strainer and the reuse tank that connects by pipeline successively, also comprises backwashing wastewater pond, sludge sump and sludge dewatering system.
The centrifugal mother liquor waste water that the PVC poly-unit produces adopts the biochemical process treatment process, and main pollution factor is:
As shown in Figure 2, centrifugal mother liquor waste water is through filtering, behind the contained resin, enter waste disposal plant in the filtering waste water, at first lower the temperature by cooling tower, then enter and clear up acidifying in the hydrolysis acidification pool, to improve the biodegradability of sewage, carry out again the Two-Stage Biochemical reaction tank and carry out biochemical aerobic treatment, enter at last settling tank and carry out mud-water separation, the clear liquid of settling tank is back to circulating water system after filtering, its effluent index is:
| pH | 6.5～8.0 |
| CODcr | ≤40 mg/l |
| BOD 5 | ≤10 mg/l |
| Ammonia nitrogen | ≤5 mg/l |
| Turbidity | ≤5NTU |
| Suspended substance | ≤10 mg/l |
| Specific conductivity | ＜350 μs/cm |
Effluent index has reached industrial circulating water moisturizing standard fully.
Be that centrifuge mother liquor passes through cooling tower successively, the Two-Stage Biochemical reaction tank, settling tank, intermediate pool and strainer, processing water after at last up to standard enters reuse tank, by pump to squeezing into the circulating water system reuse, mud in the settling tank after the precipitation enters sludge sump, mud in the sludge sump pumps into sludge dewatering system, through the outward transport of the mud cake after the dehydration, use the Two-Stage Biochemical reaction tank at sludge dewatering system processing water out by back of pipeline, the slurry that strainer filters enters the backwashing wastewater pond, and the backwashing wastewater pond pumps into Two-Stage Biochemical reaction tank recycling processing by pump with the water in the backwashing wastewater pond.
Above-mentioned chlor-alkali industrial waste water Zero discharging system adds simultaneously air blast of nutritive salt in the described Two-Stage Biochemical reaction tank, enter settling tank behind biochemical reaction, and filter, and is delivered to circulating water system when making water quality reach the recirculated water reuse standard.
As shown in Figure 4, comprehensive wastewater treatment system comprises the equalizing tank that connects successively, neutralization tank, coagulation basin, settling tank, intermediate pool, valveless water filter device and reuse tank, also comprise sludge sump, comprehensive wastewater flows into equalizing tank through grille well, equalizing tank pumps into neutralization tank, with the pH value in HCl and the NaOH adjusting neutralization tank, when the pH value is discharged in the coagulation basin during for 6-9, enter successively again intermediate pool and valveless water filter device, processing water after the filtration enters reuse tank, reuse tank is connected to the sub-salt well reuse by pipeline, the mud of settling tank precipitation pumps into comprehensive sludge sump, and air blast pumps into mother liquor unit sludge dewatering system simultaneously in the sludge sump, and the supernatant liquor in the sludge sump is fed back into equalizing tank, filtration slurry after the valveless water filter device is processed turns back to the equalizing tank circular treatment, is communicated with in intermediate pool and middle the pipe by leap of reuse tank.
Comprehensive wastewater be mainly derived from come from plant area's secondary brine and electrolysis wastewater, primary brine contains film denitration waste water, Desultwater Station waste water and ground flushing water, the water water yield designs maximum 80 m3/h, normal approximately 40-45 m3/h.Its main pollution factor is as follows:
The equalizing tank that comprehensive wastewater enters sewage treatment unit carries out the water quantity and quality adjusting, then entering neutralization tank neutralizes, at last by coagulation and precipitation, after filtering, the valveless water filter device is collected into reuse pool, and add again the oxygenant sterilization and be pumped to the light salt brine groove and return well by sending outside.Water quality such as following table after comprehensive wastewater is processed:
| The pH value | 6～9 | |
| SS | ＜10 | mg/L |
| CODcr | <50 | mg/L |
| BOD5 | ＜10 | mg/L |
| Sulfide | ＜1.0 | mg/L |
| Phosphoric acid salt | ＜0.5 | mg/L |
| Total phosphorus (with the P note) | ＜0.5 | mg/L |
| Total nitrogen (with the N note) | ＜15 | mg/L |
| Petroleum-type | ＜1 | mg/L |
This composite wastewater may exist balance not fall in other company, can go up the treatment process of a cover " ultrafiltration+reverse osmosis " herein, the light salt brine that produces through reverse osmosis is back to circulating water system, and the strong brine of residue 10-15m3/h is sent to the light salt brine groove and returns sub-salt well and adopt halogen.
As shown in Figure 3, inferior sodium Waste Water Treatment is by the gas stripping column that connects by pipeline successively, cooling tower, the first pH regulator pond, oxidation pond, the second pH regulator pond, the dephosphorization pond, settling tank, sludge sump, comprehensive unit sludge sump and sludge treating system, also comprise intermediate pool, hay tank and clean water basin, inferior sodium waste water enters cooling tower behind gas stripping column, cooling tower inferior sodium waste water out enters the first pH regulator pond, regulate pH value in the first pH regulator pond with HCl and NaOH, when the pH value is discharged in the oxidation pond during for 6-9, adding oxygenant in the oxidation pond carries out entering the second pH regulator pond after the oxidation, with the pH value in HCl and the NaOH adjusting neutralization tank, when the pH value enters the dephosphorization pond during for 6-9, be discharged into settling tank after adding the dephosphorization agent reaction, supernatant liquid enters into intermediate pool, with the pH value in HCl and the NaOH adjusting intermediate pool, when pH value 6-9, be drained into hay tank, filtered clear water is back to use sub-salt well after entering into clean water basin, backwashing wastewater after hay tank filters turns back to a pH value equalizing tank and carries out circular treatment, the slurry of settling tank lower floor pumps into sludge sump, the supernatant liquid of sludge sump turns back to a pH value equalizing tank and carries out circular treatment, the material of sludge sump lower floor enters into the comprehensive unit sludge sump and carries out sludge treatment, at a pH value equalizing tank, all send into pressurized air when the 2nd pH value equalizing tank and intermediate pool adjust pH.
Useless time sodium water is mainly from the acetylene cleaning device, and draining contains acetylene gas, and main pollution factor is as follows:
Useless sodium water is by the centrifugation of degassing tower, in the waste water main organism---acetylene gas is removed substantially; The gas stripping column water outlet promotes through the one-level lift pump and enters cooling tower, and water temperature flows into the first pH regulator pond after dropping to normal temperature certainly; In the first pH regulator pond, add acid, alkali medicament, pass into pressurized air and stir, regulate former water pH to the optimum range of oxidizing reaction requirement; 1 water outlet of pH regulator pond flows into oxidation pond, adds oxygenant in the oxidation pond, fully mixes, reacts with waste water under the effect of stirrer, the phosphate oxidation of waste water middle or low price attitude is become the orthophosphoric acid salt of high valence state; Enter the second pH regulator pond through snperoxiaized sewage, by adding the soda acid medicament, under compressed-air actuated stirring action, regulate sewage pH to the scope of dephosphorization reaction needed; The water outlet in the second pH regulator pond enters the dephosphorization pond, and in the pond with molysite reaction, the ortho-phosphoric acid root in the water is converted into throw out, and then in settling tank, precipitate and remove, establish purlin car formula suction dredger in the settling tank, the mud that in time eliminating precipitates; The settling tank water outlet enters neutralization tank, in neutralization tank pH regulator to neutral and gravity flow is entered intermediate pool; By the two-stage hoisting pump sewage lifting in the intermediate pool is entered the active carbon filtration tank, remove unnecessary oxygenant and partly remain throw out, the water outlet after the filtration enters clean water basin; The clean water basin water outlet promotes through pump and drains into waste disposal plant and always discharge the pond or be delivered to plant area's light salt brine through piping lane and return well slot; The mud of settling tank mud channel by pool side under the effect of suction dredger enters sludge sump.Sludge sump divides two lattice, and lattice are used for preliminary concentrated, and concentrated rear mud to the comprehensive unit sludge sump, jointly carries out processed with other unit mud through pump delivery; The supernatant liquor overflow is processed again through pumped back dephosphorization pond to another lattice.Effluent index was after it was processed:
| Suspended substance | <20mg/L |
| CODcr | ≤100 mg/l |
| Sulfide | <5mg/L |
| Phosphoric acid salt | ≤3 mg/l |
| pH | 6～9 |
Since return well bittern index to the requirement of inorganic amine for less than or equal to 1PPM, total amine is less than or equal to 4PPM, between the pH value 7-8, other indexs are without obvious requirement; Useless time sodium water is designed to 25 m3/h, normal 15 m3/h, and middle water COD after treatment, sulfide, phosphate content are less, and therefore returning sub-salt well, to adopt halogen feasible.
As shown in Figure 6, described sanitary wastewater treatment system comprises grille well, sanitary wastewater flows into settling pit after by grille well, lower floor's mud of settling pit pumps into comprehensive sludge sump, the supernatant liquid of settling pit enters equalizing tank and integration apparatus, enter settling tank after again processing, the supernatant liquid of settling tank enters the centrifuge mother liquor processing unit, and the lower floor of settling tank turns back to the settling pit circular treatment.
The utility model also comprises Desalting Water System and circulating water system.
As shown in Figure 5, the de-salted water device is Desalting Water System, and de-salted water NF concentrated water reuse acetylene occurs and returns well and adopt halogen, and Desalting Water System mainly adopts ultrafiltration, reverse osmosis, mixed bed production technique, and it is 160m that reverse osmosis design is processed aquifer yield
3/ h.Wherein per hour produce approximately 53m through reverse osmosis
3Dense water, saltiness is large, if directly draining, this part waste water caused the wasting of resources, we are in conjunction with company's actual process situation, design a dense water reclamation system in Desalting Water System, this part wastewater collection to dense water tank, is sent outside pump by dense water and is sent to the acetylene generation through outer piping lane, also be used for simultaneously configuration time sodium.Another part can be delivered to light salt brine through outer tube and return well slot, and alternative water returns well and adopts halogen.Can all carry out reuse through the dense water of de-salted water after the properly distributed.Also can go up a cover second level reverse osmosis apparatus, the rate of recovery is calculated by 70%, and the light salt brine of processing 45 m3/h that produce through two-pass reverse osmosis is recycled to raw water box, and the strong brine that remains 20m3/h is sent to the light salt brine groove and returns well and adopt halogen.
Reuse of Wastewater Form Circulating Cooling Water acetylene occurs: circulating water system water supply ability first phase is 16000m3/h, and the circulating water system type of cooling adopts open cycle, and its cycles of concentration is controlled N≤3.5 at present, when system's saltiness increases, need to carry out blowdown.After linking up with designing unit, set up a discharge outlet at acetylene generation recirculated water water return pipeline, be directly used in acetylene a water occurs to substitute, normal blowdown 74 m3/h of recirculated water, (the centrifugal mother liquor waste water saltiness after the processing was low, hardness is low after centrifugal mother liquor waste water was processed, can improve the recirculated water cycles of concentration, the minimizing blowdown flow rate) being back to circulating water system can be down to the Circulating water effluent amount about 40m3/h, and (120,000 tons of PVC) occurs in acetylene in direct reuse, and annual water saving is 320,000 m3 approximately.
The recovery of water of condensation and heat reuse
Desalting Water System technique is divided five processing units such as pre-treatment, reverse osmosis, precision processing, phlegma recovery, strong brine recovery, design water production rate 160m3/h, and effluent index reaches processing requirement.Because the steam that new factory of my company uses is to be provided by old factory, at a distance of 5km, phlegma is recycled to having little significance of boiler.We are back to the pure water system Pure-water Making with this part water, design phlegma recovery system.Heat is back to the heating of former water, and the former water after the heating enters Desalting Water System and is used for Pure-water Making, has improved the producing water ratio of reverse osmosis, and also having solved simultaneously affects the reverse osmosis produced water yield because water temperature in winter is low.The maximized water resources comprehensive utilization that carries out of project, and the heat of phlegma reclaimed.
Of the present utility model
The sanitary sewage technical process is schematically as follows:
One, each water processing establishment allocative abilities:
(1) former water:One time water uses Deep Underground water, produces approximately 400 m of normal water supply amount
3/ h after middle water reuse all comes into operation, can be down to 260 m
3/ h.Full factory has six industrial wells, and every well capacity of outlet water is 80m
3/ h.Because service water has critical role to Chemical Manufacture, because going wrong, cause in industrial well system to stop transport for fear of the chemical technique system.Therefore, it is capable that a received shipment is opened in industrial well employing five, to satisfy manufacture water demand.
Two) recirculated water:Mainly form by cooling tower, tower sink, water circulating pump (minute public, two systems of polymerization), priming reservoir, shallow-sand filter, chlorinating equipment, chemicals dosing plant, water monitoring device with to return pipe net, water supply capacity first phase (100,000 tons of caustic soda, 120,000 tons of PVC) is 16000m
3/ h, system possess water yield 7000m
3, undertaking the task that each interchanger of full company provides cooling water.
Three) de-salted water:Main " ultrafiltration, reverse osmosis, the mixed bed " treatment process that adopts, its designing treatment aquifer yield is 160m
3/ h, wherein to design the water yield be 240 m in ultrafiltration
3/ h, it is 160 m that reverse osmosis, mixed bed are designed outlet capacity
3/ h, the de-salted water after ultrafiltration, reverse osmosis, mixed bed desalting treatment are qualified is sent to each production and application unit of company through outer tube.
Four) sink drainage:
1, the mother liquid coming processing unit designing treatment water yield 65 m
3/ h.Year 8000 hours operating times, can designed capacity＜the lower operation of 110% load, install producing water ratio and reach more than 95%.
2, the useless time sodium unit for treating water designing treatment water yield 25 m
3/ h.Year 8000 hours operating times, can designed capacity＜110% load is lower to be operated.
3, composite wastewater processing unit designing treatment ability 80 m
3/ h, because partial drainage is intermittently discharged, design 800m
3Equalizing tank is regulated.Year 8000 hours operating times, can designed capacity＜110% load is lower to be operated.
4, the sanitary sewage cell processing designing treatment water yield 20 m
3/ h.Year 8000 hours operating times, can designed capacity＜100% load is lower to be operated.
Two, full factory reuse water situation
(1) the soda-wash tower mercury-containing waste water removes the carbide slag stock tank after processing
1. wastewater source and index:
Mercury-containing waste water is mainly derived from soda-wash tower, and index is as follows:
a)
B) process choice
Mercury-containing waste water is the difficult problem of industry wastewater treatment always, and we find a good method, is exactly by after increasing some equipment, is sent to my company's slag stock tank through outer piping lane, and the slag stock tank is making cement next, thoroughly eliminates the mercury evil.
Reaction equation: Hg2-+S2--HgS ↓
(2) centrifuge mother liquor is processed rear reuse circulating water system up to standard
The centrifugal mother liquor waste water that the PVC poly-unit produces adopts the biochemical process treatment process, and main pollution factor is:
Centrifugal mother liquor waste water is through filtering, and behind the contained resin, enters waste disposal plant in the filtering waste water.At first lower the temperature by cooling tower, then enter in the hydrolysis acidification pool pond acidifying that is hydrolyzed, to improve the biodegradability of sewage, carry out again the two-stage aerobic biochemical treatment, enter at last settling tank and carry out mud-water separation, the clear liquid of settling tank is back to circulating water system after filtering.Its effluent index is:
| pH | 6.5～8.0 |
| COD | ≤40 mg/l |
| BOD5 | ≤10 mg/l |
| Ammonia nitrogen | ≤5 mg/l |
| Turbidity | ≤5NTU |
| Suspended substance | ≤10 mg/l |
| Specific conductivity | ＜350 μs/cm |
Effluent index has reached industrial circulating water moisturizing standard fully.
(3) the useless time qualified rear reuse light salt brine groove of sodium water treatment returns well and adopts halogen
Useless time sodium water is mainly from the acetylene cleaning device, and draining contains acetylene gas, and main pollution factor is as follows:
Useless sodium water is by the centrifugation of degassing tower, in the waste water main organism---acetylene gas is removed substantially; The gas stripping column water outlet promotes through the one-level lift pump and enters cooling tower, and water temperature flows into pH regulator pond 1 after dropping to normal temperature certainly; In pH regulator pond 1, add acid, alkali medicament, pass into pressurized air and stir, regulate former water pH to the optimum range of oxidizing reaction requirement; 1 water outlet of pH regulator pond flows into oxidation pond, adds oxygenant in the oxidation pond, fully mixes, reacts with waste water under the effect of stirrer, the phosphate oxidation of waste water middle or low price attitude is become the orthophosphoric acid salt of high valence state; Enter pH regulator pond 2 through snperoxiaized sewage, by adding the soda acid medicament, under compressed-air actuated stirring action, regulate sewage pH to the scope of dephosphorization reaction needed; The water outlet in pH regulator pond 2 enters the dephosphorization pond, and in the pond with molysite reaction, the ortho-phosphoric acid root in the water is converted into throw out, and then in settling tank, precipitate and remove, establish purlin car formula suction dredger in the settling tank, the mud that in time eliminating precipitates; The settling tank water outlet enters neutralization tank, in neutralization tank pH regulator to neutral and gravity flow is entered intermediate pool; By the two-stage hoisting pump sewage lifting in the intermediate pool is entered the active carbon filtration tank, remove unnecessary oxygenant and partly remain throw out, the water outlet after the filtration enters clean water basin; The clean water basin water outlet promotes through pump and drains into waste disposal plant and always discharge the pond or be delivered to plant area's light salt brine through piping lane and return well slot; The mud of settling tank mud channel by pool side under the effect of suction dredger enters sludge sump.Sludge sump divides two lattice, and lattice are used for preliminary concentrated, and concentrated rear mud to the comprehensive unit sludge sump, jointly carries out processed with other unit mud through pump delivery; The supernatant liquor overflow is processed again through pumped back dephosphorization pond to another lattice.Effluent index was after it was processed:
| Suspended substance | <20mg/L |
| COD | ≤100 mg/l |
| Sulfide | <5mg/L |
| Phosphoric acid salt | ≤3 mg/l |
| pH | 6～9 |
Since return well bittern index to the requirement of inorganic amine for less than or equal to 1PPM, total amine is less than or equal to 4PPM, between the pH value 7-8, other indexs are without obvious requirement; Useless time sodium water is designed to 25 m3/h, normal 15 m3/h, and middle water COD after treatment, sulfide, phosphate content are less, and therefore returning well, to adopt halogen feasible.
(4) de-salted water NF concentrated water reuse acetylene occurs and returns well and adopt halogen
Desalting Water System mainly adopts ultrafiltration, reverse osmosis, mixed bed production technique, and it is 160m3/h that reverse osmosis design is processed aquifer yield.Wherein per hour produce the approximately dense water of 65m3 through reverse osmosis, saltiness is large, if directly draining, this part waste water caused the wasting of resources, we are in conjunction with company's actual process situation, design a dense water reclamation system in Desalting Water System, this part wastewater collection to dense water tank, is sent outside pump by dense water and is sent to the acetylene generation through outer piping lane, also be used for simultaneously configuration time sodium.Another part can be delivered to light salt brine through outer tube and return well slot, and alternative water returns well and adopts halogen.Can all carry out reuse through the dense water of de-salted water after the properly distributed.Also can go up a cover second level reverse osmosis apparatus, the rate of recovery is calculated by 70%, and the light salt brine of processing 45 m3/h that produce through two-pass reverse osmosis is recycled to raw water box, and the strong brine that remains 20m3/h is sent to the light salt brine groove and returns well and adopt halogen.
(5) Reuse of Wastewater Form Circulating Cooling Water acetylene occurs
Circulating water system water supply ability first phase is 16000m3/h, and the circulating water system type of cooling adopts open cycle, and its cycles of concentration is controlled N≤3.5 at present, when system's saltiness increases, need to carry out blowdown.After linking up with designing unit, set up a discharge outlet at acetylene generation recirculated water water return pipeline, be directly used in acetylene a water occurs to substitute, normal blowdown 74 m3/h of recirculated water, (the centrifugal mother liquor waste water saltiness after the processing was low, hardness is low after centrifugal mother liquor waste water was processed, can improve the recirculated water cycles of concentration, the minimizing blowdown flow rate) being back to circulating water system can be down to the Circulating water effluent amount about 40m3/h, and (120,000 tons of PVC) occurs in acetylene in direct reuse, and annual water saving is 320,000 m3 approximately.
(6) recovery of water of condensation and heat reuse
Desalting Water System technique is divided five processing units such as pre-treatment, reverse osmosis, precision processing, phlegma recovery, strong brine recovery, design water production rate 160m3/h, and effluent index reaches processing requirement.Because the steam that new factory of my company uses is to be provided by old factory, at a distance of 5km, phlegma is recycled to having little significance of boiler.We are back to the pure water system Pure-water Making with this part water, design phlegma recovery system.Heat is back to the heating of former water, and the former water after the heating enters Desalting Water System and is used for Pure-water Making, has improved the producing water ratio of reverse osmosis, and also having solved simultaneously affects the reverse osmosis produced water yield because water temperature in winter is low.The maximized water resources comprehensive utilization that carries out of project, and the heat of phlegma reclaimed.
(7) comprehensive wastewater is processed qualified rear reuse and is adopted halogen
Comprehensive wastewater be mainly derived from come from plant area's secondary brine and electrolysis wastewater, primary brine contains film denitration waste water, Desultwater Station waste water and ground flushing water, the water water yield designs maximum 80 m3/h, normal approximately 40-45 m3/h.Its main pollution factor is as follows:
The equalizing tank that comprehensive wastewater enters sewage treatment unit carries out the water quantity and quality adjusting, then entering neutralization tank neutralizes, at last by coagulation and precipitation, after filtering, the valveless water filter device is collected into reuse pool, and add again the oxygenant sterilization and be pumped to the light salt brine groove and return well by sending outside.Water quality such as following table after comprehensive wastewater is processed:
| The pH value | 6～9 | |
| SS | ＜10 | mg/L |
| COD | <50 | mg/L |
| BOD5 | ＜10 | mg/L |
| Sulfide | ＜1.0 | mg/L |
| Phosphoric acid salt | ＜0.5 | mg/L |
| Total phosphorus (with the P note) | ＜0.5 | mg/L |
| Total nitrogen (with the N note) | ＜15 | mg/L |
| Petroleum-type | ＜1 | mg/L |
This composite wastewater may exist balance not fall in other company, can go up the treatment process of a cover " ultrafiltration+reverse osmosis " herein, and the light salt brine that produces through reverse osmosis is back to circulating water system, and the strong brine of residue 10-15m3/h is sent to the light salt brine groove and returns well and adopt halogen.
Claims (10)
1. chlor-alkali industrial waste water Zero discharging system, comprise time sodium Waste Water Treatment, the centrifuge mother liquor treatment system, comprehensive wastewater treatment system, domestic sewage processing system and circulating water system, it is characterized in that: well water is transported to soda equipment with the de-salted water of producing after processing by the de-salted water device, the PVC poly-unit is for production and application, the strong brine part that the de-salted water device produces is used for carbide-feed generator, a part is sent into the light salt brine groove and is returned sub-salt well and adopt halogen, the water of productive use station owner will supply the acetylene cleaning device, PVC polymerization generating apparatus, soda equipment and acetylene section soda-wash tower use, after time sodium Waste Water Treatment processing is up to standard, be back to sub-salt well from acetylene cleaning device inferior sodium waste water out and be used for adopting halogen, after the processing of centrifuge mother liquor treatment system is up to standard, be back to circulating water system from PVC polymerization generating apparatus centrifuge mother liquor out, from PVC polymerization generating apparatus out factory effluent and process through comprehensive wastewater treatment system from soda equipment factory effluent out and to be back to sub-salt well after up to standard and to be used for light salt brine and to adopt halogen, water in water circulating system with water is back to use carbide-feed generator, enter the centrifuge mother liquor processing unit after domestic water is processed by the sanitary wastewater treatment system and carry out advanced treatment, be back to circulating water system after qualified.
2. chlor-alkali industrial waste water Zero discharging system according to claim 1 is characterized in that: also comprise slag stock tank treatment system, acetylene section soda-wash tower mercury-containing waste water out is used for cement plant and is made into cement after slag stock tank treatment system is processed.
3. chlor-alkali industrial waste water Zero discharging system according to claim 1 and 2, it is characterized in that: described centrifuge mother liquor treatment system comprises the cooling tower that connects by pipeline successively, the Two-Stage Biochemical reaction tank, settling tank, intermediate pool, strainer and reuse tank, also comprise the backwashing wastewater pond, sludge sump and sludge dewatering system, centrifuge mother liquor passes through cooling tower successively, the Two-Stage Biochemical reaction tank, settling tank, intermediate pool and strainer, processing water after at last up to standard enters reuse tank, by pump to squeezing into the circulating water system reuse, mud in the settling tank after the precipitation enters sludge sump, mud in the sludge sump pumps into sludge dewatering system, through the outward transport of the mud cake after the dehydration, use the Two-Stage Biochemical reaction tank at sludge dewatering system processing water out by back of pipeline, the slurry that strainer filters enters the backwashing wastewater pond, and the backwashing wastewater pond pumps into Two-Stage Biochemical reaction tank recycling processing by pump with the water in the backwashing wastewater pond.
4. chlor-alkali industrial waste water Zero discharging system according to claim 3, it is characterized in that: add simultaneously air blast of nutritive salt in the described Two-Stage Biochemical reaction tank, behind biochemical reaction, enter settling tank, and filter and be delivered to circulating water system when making water quality reach the recirculated water reuse standard.
5. chlor-alkali industrial waste water Zero discharging system according to claim 4, it is characterized in that: described comprehensive wastewater treatment system comprises the equalizing tank that connects successively, neutralization tank, coagulation basin, settling tank, intermediate pool, valveless water filter device and reuse tank, also comprise sludge sump, comprehensive wastewater flows into equalizing tank through grille well, equalizing tank pumps into neutralization tank, with the pH value in HCl and the NaOH adjusting neutralization tank, when the pH value is discharged in the coagulation basin during for 6-9, enter successively again intermediate pool and valveless water filter device, processing water after the filtration enters reuse tank, reuse tank is connected to the sub-salt well reuse by pipeline, the mud of settling tank precipitation pumps into comprehensive sludge sump, air blast pumps into mother liquor unit sludge dewatering system simultaneously in the sludge sump, supernatant liquor in the sludge sump turns back to equalizing tank, and the filtration slurry after the valveless water filter device is processed turns back to the equalizing tank circular treatment.
6. chlor-alkali industrial waste water Zero discharging system according to claim 5 is characterized in that: be communicated with in intermediate pool and middle the pipe by leap of reuse tank.
7. chlor-alkali industrial waste water Zero discharging system according to claim 6, it is characterized in that: described sodium Waste Water Treatment is by the gas stripping column that connects by pipeline successively, cooling tower, the first pH regulator pond, oxidation pond, the second pH regulator pond, the dephosphorization pond, settling tank, sludge sump, comprehensive sludge sump and sludge treating system, also comprise intermediate pool, hay tank and clean water basin, inferior sodium waste water enters cooling tower behind gas stripping column, cooling tower inferior sodium waste water out enters the first pH regulator pond, regulate pH value in the first pH regulator pond with HCl and NaOH, when the pH value is discharged in the oxidation pond during for 6-9, adding oxygenant in the oxidation pond carries out entering the second pH regulator pond after the oxidation, with the pH value in HCl and the NaOH adjusting neutralization tank, when the pH value enters the dephosphorization pond during for 6-9, be discharged into settling tank after adding the dephosphorization agent reaction, supernatant liquid enters into intermediate pool, with the pH value in HCl and the NaOH adjusting intermediate pool, when pH value 6-7, be drained into hay tank, filtered clear water is back to use sub-salt well after entering into clean water basin, backwashing wastewater after hay tank filters turns back to a pH value equalizing tank and carries out circular treatment, the slip of settling tank lower floor pumps into sludge sump, the supernatant liquid of sludge sump turns back to a pH value equalizing tank and carries out circular treatment, and the material of sludge sump lower floor enters into comprehensive sludge sump and carries out sludge treatment.
8. chlor-alkali industrial waste water Zero discharging system according to claim 7 is characterized in that: all send into pressurized air when a pH value equalizing tank, the 2nd pH value equalizing tank and intermediate pool adjust pH.
9. chlor-alkali industrial waste water Zero discharging system according to claim 8, it is characterized in that: described sanitary wastewater treatment system comprises grille well, sanitary wastewater flows into settling pit after by grille well, lower floor's mud of settling pit pumps into comprehensive sludge sump, the supernatant liquid of settling pit enters equalizing tank and integration apparatus, enter settling tank after again processing, the supernatant liquid of settling tank enters the centrifuge mother liquor processing unit, and the lower floor of settling tank turns back to the settling pit circular treatment.
10. chlor-alkali industrial waste water Zero discharging system according to claim 9, it is characterized in that: described de-salted water device comprises five processing units such as pre-treatment, reverse osmosis, precision processing, phlegma recovery, strong brine recovery.
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|---|---|---|---|
| CN 201220507198 CN202865020U (en) | 2012-09-29 | 2012-09-29 | Chlor-alkali industrial wastewater zero discharge system |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201220507198 CN202865020U (en) | 2012-09-29 | 2012-09-29 | Chlor-alkali industrial wastewater zero discharge system |
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Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102964024A (en) * | 2012-09-29 | 2013-03-13 | 河南永银化工实业有限公司 | Wastewater zero discharge system of chlorine-alkali industry |
| CN107585968A (en) * | 2017-10-25 | 2018-01-16 | 陕西北元化工集团股份有限公司 | A kind of chlor-alkali brine waste processing system and method |
| CN108726798A (en) * | 2018-05-31 | 2018-11-02 | 青海盐湖工业股份有限公司 | A kind of waste water utilization system |
| CN113003771A (en) * | 2021-03-08 | 2021-06-22 | 西安交通大学 | Comprehensive treatment system for recycling of salt mud in chlor-alkali industry |
-
2012
- 2012-09-29 CN CN 201220507198 patent/CN202865020U/en not_active Withdrawn - After Issue
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102964024A (en) * | 2012-09-29 | 2013-03-13 | 河南永银化工实业有限公司 | Wastewater zero discharge system of chlorine-alkali industry |
| CN107585968A (en) * | 2017-10-25 | 2018-01-16 | 陕西北元化工集团股份有限公司 | A kind of chlor-alkali brine waste processing system and method |
| CN107585968B (en) * | 2017-10-25 | 2019-10-11 | 陕西北元化工集团股份有限公司 | A kind of chlor-alkali brine waste processing system and method |
| CN108726798A (en) * | 2018-05-31 | 2018-11-02 | 青海盐湖工业股份有限公司 | A kind of waste water utilization system |
| CN113003771A (en) * | 2021-03-08 | 2021-06-22 | 西安交通大学 | Comprehensive treatment system for recycling of salt mud in chlor-alkali industry |
| CN113003771B (en) * | 2021-03-08 | 2022-06-07 | 西安交通大学 | Comprehensive treatment system for recycling of salt mud in chlor-alkali industry |
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