CN106830492A - A kind of processing method of methoxy acrylic Pesticidal products waste water - Google Patents

A kind of processing method of methoxy acrylic Pesticidal products waste water Download PDF

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Publication number
CN106830492A
CN106830492A CN201710217270.1A CN201710217270A CN106830492A CN 106830492 A CN106830492 A CN 106830492A CN 201710217270 A CN201710217270 A CN 201710217270A CN 106830492 A CN106830492 A CN 106830492A
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waste water
processing method
potassium
methoxy acrylic
pesticidal products
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CN106830492B (en
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尚鸿艳
孙敬权
李新生
张荣全
庄文栋
孙丽梅
冯小冬
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Limin Chemical Co.,Ltd.
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LIMIN CHEMICAL CO Ltd
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    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F9/00Multistage treatment of water, waste water or sewage
    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01DCOMPOUNDS OF ALKALI METALS, i.e. LITHIUM, SODIUM, POTASSIUM, RUBIDIUM, CAESIUM, OR FRANCIUM
    • C01D5/00Sulfates or sulfites of sodium, potassium or alkali metals in general
    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01DCOMPOUNDS OF ALKALI METALS, i.e. LITHIUM, SODIUM, POTASSIUM, RUBIDIUM, CAESIUM, OR FRANCIUM
    • C01D5/00Sulfates or sulfites of sodium, potassium or alkali metals in general
    • C01D5/02Preparation of sulfates from alkali metal salts and sulfuric acid or bisulfates; Preparation of bisulfates
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/001Processes for the treatment of water whereby the filtration technique is of importance
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/02Treatment of water, waste water, or sewage by heating
    • C02F1/04Treatment of water, waste water, or sewage by heating by distillation or evaporation
    • C02F1/048Purification of waste water by evaporation
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/30Treatment of water, waste water, or sewage by irradiation
    • C02F1/32Treatment of water, waste water, or sewage by irradiation with ultraviolet light
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/52Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities
    • C02F1/5236Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities using inorganic agents
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/66Treatment of water, waste water, or sewage by neutralisation; pH adjustment
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/72Treatment of water, waste water, or sewage by oxidation
    • C02F1/725Treatment of water, waste water, or sewage by oxidation by catalytic oxidation
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2101/00Nature of the contaminant
    • C02F2101/10Inorganic compounds
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2101/00Nature of the contaminant
    • C02F2101/30Organic compounds
    • C02F2101/40Organic compounds containing sulfur
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2103/00Nature of the water, waste water, sewage or sludge to be treated
    • C02F2103/34Nature of the water, waste water, sewage or sludge to be treated from industrial activities not provided for in groups C02F2103/12 - C02F2103/32
    • C02F2103/343Nature of the water, waste water, sewage or sludge to be treated from industrial activities not provided for in groups C02F2103/12 - C02F2103/32 from the pharmaceutical industry, e.g. containing antibiotics
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2103/00Nature of the water, waste water, sewage or sludge to be treated
    • C02F2103/34Nature of the water, waste water, sewage or sludge to be treated from industrial activities not provided for in groups C02F2103/12 - C02F2103/32
    • C02F2103/36Nature of the water, waste water, sewage or sludge to be treated from industrial activities not provided for in groups C02F2103/12 - C02F2103/32 from the manufacture of organic compounds
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2301/00General aspects of water treatment
    • C02F2301/08Multistage treatments, e.g. repetition of the same process step under different conditions

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  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Engineering & Computer Science (AREA)
  • Materials Engineering (AREA)
  • Inorganic Chemistry (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Hydrology & Water Resources (AREA)
  • Environmental & Geological Engineering (AREA)
  • Water Supply & Treatment (AREA)
  • Separation Of Suspended Particles By Flocculating Agents (AREA)
  • Treatment Of Water By Oxidation Or Reduction (AREA)

Abstract

The present invention relates to a kind of processing method of methoxy acrylic Pesticidal products waste water, the described method comprises the following steps:Wastewater collection is simultaneously filtered;Sulfuric acid is added, pH value is adjusted, and inorganic potassium salt is converted into potassium sulfate;UV photochemical catalytic oxidations, make potassium salt be converted into potassium sulfate;Potassium hydroxide is added, pH value is adjusted, and neutralizes excessive sulfuric acid, being subsequently adding ferric trichloride carries out precipitation reaction;Filtering, removes flocculate;Multiple-effect evaporation simultaneously crystallizes centrifugation, isolated potassium sulfate solid, steam condensate (SC) and steams water and is back to workshop.Realize utilization of wastewater resource, wastewater zero discharge, with energy economy & environment benefit higher.

Description

A kind of processing method of methoxy acrylic Pesticidal products waste water
Technical field
The present invention relates to technical field of waste water processing, specifically, it is related to a kind of methoxy acrylic Pesticidal products The processing method of waste water.
Background technology
Production methoxy acrylic Pesticidal products such as pyraclostrobin, Fluoxastrobin, kresoxim-methyl, trifloxystrobin etc., are produced Raw waste water main component is:Active compound, potassium methyl sulfate, potassium carbonate, saleratus mixed salt, CODcr=30000-40000mg/ l。
For high-salt wastewater, the Processing tecchnics that current manufacturing enterprise generally uses for:The first step:Product is reclaimed in press filtration;The Two steps, evaporate desalination:Steam water CODcr=5000-10000mg/l, it is necessary to further treatment after qualified discharge, mixed salt is used as danger Dangerous waste commission disposal.
There is problems with conventional processes:
1) because waste water COD cr concentration is higher, the mixed salt for obtaining directly is evaporated without pretreatment can only be used as hazardous waste Disposal, while greatly increasing cost of disposal, wastes useful resources.
2) steam water still containing organic matter higher, need to by after further treatment can qualified discharge, processing cost is higher, And do not produce economic benefit.
The content of the invention
In order to solve the deficiency of prior art presence, it is an object of the invention to provide a kind of methoxy acrylic agriculture The processing method of medicine product waste water, realizes the recycling of Coal Gas Washing Cycling Water saliferous high, and production potassium sulfate is used as byproduct Sell, steam condensate (SC) and steam water and be back to workshop, tail gas qualified discharge after Alkali absorption does not produce secondary pollution, tool There is good energy economy & environment benefit.
To achieve the above object, the present invention provides a kind of processing method of methoxy acrylic Pesticidal products waste water, Comprise the following steps:
1) wastewater collection and filter;
2) sulfuric acid is added, pH value is adjusted, and inorganic potassium salt is converted into potassium sulfate;
3) UV- photochemical catalytic oxidations, make potassium salt be converted into potassium sulfate;
4) potassium hydroxide is added, pH value is adjusted, and neutralizes excessive sulfuric acid, being subsequently adding ferric trichloride carries out flocculation sediment Reaction;
5) filter, remove flocculate;
6) multiple-effect evaporation and centrifugation is crystallized, isolated potassium sulfate solid and steams water and is back to car steam condensate (SC) Between.
Further, the step 1) in filtration step use duplex strainer.
Further, the step 2) in regulation pH value be 2.5-3.0.
Further, the step 2) in inorganic potassium salt be potassium carbonate and saleratus, reaction equation is as follows:
K2CO3+H2SO4→K2SO4+H2O+CO2
2KHCO3+H2SO4→K2SO4+2H2O+2CO2↑。
Further, the step 3) in potassium salt be potassium methyl sulfate, reaction equation is as follows:
R-H+HO·→R·+H2O
2K(CH3)SO4+3O2→K2SO4+2H2O+2CO2↑+H2SO4
Further, the step 4) in regulation pH value be 6.0-7.0.
Further, the step 4) in reaction equation it is as follows:
H2SO4+2KOH→K2SO4+2H2O
3KOH+FeCl3→Fe(OH)3↓+3KCl。
Further, the step 5) in flocculate include the small organic molecule that can flocculate of iron hydroxide and small part.
Further, the step 2) and step 3) in reaction generation gas and the step 6) in evaporation process produce Gas through Alkali absorption process.
Further, the Alkali absorption is carried out using two-stage spray column, and the alkali in the Alkali absorption is NaOH water Solution or aqueous sodium carbonate.
Compared with prior art, the present invention has advantages below:
1) reclaim product process and traditional press filtration is replaced using duplex strainer, operation is easier, substantially improves site environment.
2) single potassium sulfate salt is changed into by potassium carbonate and saleratus mixed salt to waste water acid adjustment, using UV- photocatalytic-oxidations Potassium methyl sulfate is changed into potassium sulfate by change technology, realizes the transformation of mixed salt in waste water to single salt, make originally as dangerous waste at The mixed salt put being capable of resource recovery.
3) whole flow process wastewater zero discharge, realizes recycling economy purpose:Sylvite is reclaimed and sold as byproduct in waste water, female Liquid set steams, and steam condensate (SC) and steams Water circulation in workshop, greatlys save water resource.
To sum up, the present invention provides a kind of processing method of methoxy acrylic Pesticidal products waste water, in realizing waste water The recycling of high concentration saliferous high, to good waste water treatment effect, efficiently solve high cost that existing treatment technology is present, Deficiency that is inefficient, producing a large amount of dangerous wastes.The purpose of waste water reclaiming, energy saving and water resource are realized, it is economical to be imitated with environmental protection It is beneficial mutually unified.
Brief description of the drawings
Fig. 1 is the process chart of methoxy acrylic Pesticidal products wastewater treatment of the invention.
Specific embodiment
In order to preferably explain the present invention, below in conjunction with the accompanying drawings and specific embodiment the invention will be further described.
As shown in figure 1, methoxy acrylic Pesticidal products, 7.2%-7.5% containing 1.3%-1.5% in waste water Potassium methyl sulfate, the saleratus of 4.8%-5.0%, the potassium carbonate of 1.4%-1.6%.
Embodiment 1
The first step, wastewater collection and is recovered by filtration product:Workshop produces 38 tons of waste water daily, and waste water enters wastewater collection Tank, tank bottom is taper, and waste water pump discharge sets duplex strainer for product to be recovered by filtration, daily 0.5 ton of recyclable product, duplex Filter sets pressure interlock control, when a pressure alarm high and switches another, it is to avoid block influence handling process continuous Change, 37.5 tons of filtrate is produced daily, into second step treatment.
Second step, adjusts pH:Waste water is with 3.0m3/ h amounts are pumped into pH regulation tanks, while 98% sulfuric acid is added, according to quality Flowmeter control acid and the ratio of waste water, sulphuric acid is 114kg/h, automatically adjusts pH=2.5, makes potassium carbonate in waste water (45kg/h) and potassium hydrogen carbonate (145kg/h) reaction generation potassium sulfate (178kg/h), tail gas introduce alkali cleaning and spray through induced draught system Drench tower treatment.
3rd step, UV- photochemical catalytic oxidations:The waste water of pH=2.5 is with 3.2m3/ h amounts pump into UV- photochemical catalytic oxidation techniques system System, is pre-processed to waste water, and 27.5% hydrogen peroxide and 40% liquor ferri trichloridi, dosage are put into using automatic medicament feeding system Respectively 1500ppm, 170ppm, are CO by organic matter degradation by the oxidation of hydroxyl radical free radical2、H2O and small molecule acid, Potassium methyl sulfate (220kg/h) is oxidized generation potassium sulfate (128kg/h), and tail gas is introduced at alkali wash spray tower through induced draught system Reason.
4th step, adjusts pH:Upper step waste water is with 3.3m3/ h amounts pump into pH regulation tanks, with 40% potassium hydroxide and waste water, The ratio of potassium hydroxide solution and waste water is controlled according to mass flowmenter, 40% potassium hydroxide dosage is 270kg/h, automatic to adjust Section makes wastewater pH=6.0, while unnecessary sulfuric acid (72kg/h) is reacted generation potassium sulfate (128kg/h), with UV- photocatalytic-oxidations Change micro ferric trichloride (0.025kg/h) reaction generation iron hydroxide (0.015kg/h) and chlorination that automatic medicament feeding system is added Potassium (0.035kg/h).
5th step, filtering and impurity removing:Small part flocculate (0.025kg/h) filtering of generation will be reacted, flocculate includes hydrogen Iron oxide and the small organic molecule that can be flocculated on a small quantity.
6th step, multiple-effect evaporation and centrifugation:The waste water of the pH=6.0 after being processed through first five step is with 3.3m3/ h measures pump Enter multi-effect evaporation system, the 434kg/h K of reaction generation are contained in waste water2SO4With 0.035kg/h KCl, waste water generation per ton KCl 0.011kg, and waste water per ton contains K2SO4131.5kg, KCl only account for the 0.008% of total salt amount, therefore the KCl for producing does not influence By-product K2SO4Quality.Under vacuum conditions, supersaturated potassium sulfate solution is concentrated to give by one, two, triple effect evaporator, then Into crystallization kettle crystallization, then it is centrifuged, obtains potassium sulfate (490kg/h, content >=85%) sold as byproduct, steam Condensed water and steam water (2.4m3/ h, CODcr≤500mg/1, NH3- N≤30mg/l) workshop is back to, evaporation process is produced Not coagulate tail gas through induced draught system introduce alkali wash spray tower process.
Alkali in the alkali wash spray tower treatment being related in step 2, three, six is the sodium hydrate aqueous solution of 2-5%.
Embodiment 2
The first step, with embodiment 1.
Second step, adjusts pH:Waste water is with 3.2m3/ h amounts are pumped into pH regulation tanks, while 80% Waste Sulfuric Acid is added, according to matter Amount flowmeter control acid and the ratio of waste water, sulphuric acid is 150kg/h, automatically adjusts pH=2.8, makes potassium carbonate in waste water (46kg/h) and potassium hydrogen carbonate (150kg/h) reaction generation potassium sulfate (190kg/h), tail gas introduce alkali cleaning and spray through induced draught system Drench tower treatment.
3rd step, UV- photochemical catalytic oxidations:The waste water of pH=2.8 is with 3.3m3/ h amounts pump into UV- photochemical catalytic oxidation techniques system System, is pre-processed to waste water, and 30% hydrogen peroxide and 35% liquor ferri trichloridi, dosage point are put into using automatic medicament feeding system Not Wei 1450ppm, 200ppm, by organic matter degradation be CO by the oxidation of hydroxyl radical free radical2、H2O and small molecule acid, first Base potassium sulfate (223kg/h) is oxidized generation potassium sulfate (130kg/h), and tail gas introduces alkali wash spray tower and processes through induced draught system.
4th step, adjusts pH:Upper step waste water is with 3.3m3/ h amounts pump into pH regulation tanks, with 38% potassium hydroxide and waste water, The ratio of potassium hydroxide solution and waste water is controlled according to mass flowmenter, 38% potassium hydroxide dosage is 290kg/h, automatic to adjust Section makes wastewater pH=6.5, while unnecessary sulfuric acid (94kg/h) is reacted generation potassium sulfate (130kg/h), with UV- photocatalytic-oxidations Change micro ferric trichloride (0.026kg/h) reaction generation iron hydroxide (0.017kg/h) and chlorination that automatic medicament feeding system is added Potassium (0.036kg/h).
5th step, filtering and impurity removing:Small part flocculate (0.026kg/h) filtering of generation will be reacted, flocculate includes hydrogen Iron oxide and the small organic molecule that can be flocculated on a small quantity.
6th step, multiple-effect evaporation and centrifugation:The waste water of the pH=6.5 after being processed through first five step is with 3.3m3/ h measures pump Enter multi-effect evaporation system, the 450kg/h K of reaction generation are contained in waste water2SO4With 0.036kg/h KCl, waste water generation per ton KCl 0.011kg, and waste water per ton contains K2SO4136.4kg, KCl only account for the 0.008% of total salt amount, therefore the KCl for producing does not influence By-product K2SO4Quality.Under vacuum conditions, supersaturated potassium sulfate solution is concentrated to give by one, two, triple effect evaporator, then Into crystallization kettle crystallization, then it is centrifuged, obtains potassium sulfate (498kg/h, content >=85%) sold as byproduct, steam Condensed water and steam water (2.5m3/ h, CODcr≤500mg/l, NH3- N≤30mg/l) workshop is back to, evaporation process is produced Not coagulate tail gas through induced draught system introduce alkali wash spray tower process.
Alkali in the alkali wash spray tower treatment being related in step 2, three, six is the aqueous sodium carbonate of 5-15%.
Embodiment 3
The first step, with embodiment 1.
Second step, adjusts pH:Waste water is with 3.2m3/ h amounts are pumped into pH regulation tanks, while 98% sulfuric acid is added, according to quality Flowmeter control acid and the ratio of waste water, sulphuric acid is 125kg/h, automatically adjusts pH=3.0, makes potassium carbonate in waste water (48kg/h) and potassium hydrogen carbonate (152kg/h) reaction generation potassium sulfate (193kg/h), tail gas introduce alkali cleaning and spray through induced draught system Drench tower treatment.
3rd step, UV- photochemical catalytic oxidations:The waste water of pH=3.0 is with 3.3m3/ h amounts pump into UV- photochemical catalytic oxidation techniques system System, is pre-processed to waste water, and 30% hydrogen peroxide and 50% liquor ferri trichloridi, dosage point are put into using automatic medicament feeding system Not Wei 1400ppm, 150ppm, by organic matter degradation be CO by the oxidation of hydroxyl radical free radical2、H2O and small molecule acid, first Base potassium sulfate (225kg/h) is oxidized generation potassium sulfate (131kg/h), and tail gas introduces alkali wash spray tower and processes through induced draught system.
4th step, adjusts pH:Upper step waste water is with 3.3m3/ h amounts pump into pH regulation tanks, with 40% potassium hydroxide and waste water, The ratio of potassium hydroxide solution and waste water is controlled according to mass flowmenter, 40% potassium hydroxide dosage is 280kg/h, automatic to adjust Section makes wastewater pH=7.0, while unnecessary sulfuric acid (74kg/h) is reacted generation potassium sulfate (131kg/h), with UV- photocatalytic-oxidations Change micro ferric trichloride (0.03kg/h) reaction generation iron hydroxide (0.02kg/h) and potassium chloride that automatic medicament feeding system is added (0.04kg/h)。
5th step, filtering and impurity removing:Small part flocculate (0.03kg/h) filtering of generation will be reacted, flocculate includes hydrogen-oxygen Change iron and the small organic molecule that can be flocculated on a small quantity.
6th step, multiple-effect evaporation and centrifugation:The waste water of the pH=7.0 after being processed through first five step is with 3.3m3/ h measures pump Enter multi-effect evaporation system, the 455kg/h K of reaction generation are contained in waste water2SO4With 0.04kg/h KCl, waste water generation KCl per ton 0.012kg, and waste water per ton contains K2SO4142kg, KCl only account for the 0.008% of total salt amount, therefore the KCl for producing does not influence by-product K2SO4Quality.Under vacuum conditions, supersaturated potassium sulfate solution is concentrated to give by one, two, triple effect evaporator, subsequently into Crystallization kettle is crystallized, then is centrifuged, and obtains potassium sulfate (510kg/h, content >=85%) sold as byproduct, steam condensation Water and steam water (2.5m3/ h, CODcr≤500mg/l, NH3- N≤30mg/l) workshop is back to, evaporation process is produced not Solidifying tail gas introduces alkali wash spray tower and processes through induced draught system.
Alkali in the alkali wash spray tower treatment being related in step 2, three, six is the sodium hydrate aqueous solution of 5-10%.
Embodiment 4
Present invention process is compared with conventional processes, with embodiment 1-3 mean consumptions as foundation, it is comprehensively imitated Benefit is analyzed, as a result as shown in table 1.
The comprehensive benefit analysis of table 1 (press the conversion of ton waste water)
Processing procedure Conventional processes Present invention process
Product is recovered by filtration Press filtration Duplex is filtered
Regulation pH /
UV- photochemical catalytic oxidations / - 100 yuan
Regulation pH / 40%KOH 83.4kg, -83 yuan
Filtering and impurity removing / /
Multiple-effect evaporation and centrifugation - 180 yuan - 150 yuan
Steam water process - 100 yuan Save water 750kg, 1.7 yuan
Dangerous waste treatment/byproduct is reclaimed 220kg dangerous wastes, -660 yuan
Integrated cost/benefit - 940 yuan - 40.3 yuan
According to the analysis result that table 1 is obtained, according to year treatment 1.2 ten thousand tons of meters of waste water, present invention process is compared with conventional process side Cost-saved 1079.6 ten thousand yuan of formula, realizes the purpose of waste water reclaiming, energy saving and water resource.
Although some exemplary embodiments of the invention have shown and described, those skilled in the art should know Dawn, without departing from the principles and spirit of the present invention, change can be made to these exemplary embodiments, it is of the invention Scope is limited by claim and its equivalent.

Claims (10)

1. a kind of processing method of methoxy acrylic Pesticidal products waste water, the described method comprises the following steps:
1) wastewater collection and filter;
2) sulfuric acid is added, pH value is adjusted, and inorganic potassium salt is converted into potassium sulfate;
3) UV- photochemical catalytic oxidations, make potassium salt be converted into potassium sulfate;
4) potassium hydroxide is added, pH value is adjusted, and excessive sulfuric acid is neutralized, being subsequently adding ferric trichloride, to carry out flocculation sediment anti- Should;
5) filter, remove flocculate;
6) multiple-effect evaporation and centrifugation is crystallized, isolated potassium sulfate solid and steams water and is back to workshop steam condensate (SC).
2. the processing method of methoxy acrylic Pesticidal products waste water according to claim 1, it is characterised in that institute State step 1) in filtration step use duplex strainer.
3. the processing method of methoxy acrylic Pesticidal products waste water according to claim 1, it is characterised in that institute State step 2) in regulation pH value be 2.5-3.0.
4. the processing method of methoxy acrylic Pesticidal products waste water according to claim 1, it is characterised in that institute State step 2) in inorganic potassium salt for potassium carbonate and saleratus, reaction equation is as follows:
K2CO3+H2SO4→K2SO4+H2O+CO2
2KHCO3+H2SO4→K2SO4+2H2O+2CO2↑。
5. the processing method of methoxy acrylic Pesticidal products waste water according to claim 1, it is characterised in that institute State step 3) in potassium salt for potassium methyl sulfate, reaction equation is as follows:
2K(CH3)SO4+3O2→K2SO4+2H2O+2CO2↑+H2SO4
6. the processing method of methoxy acrylic Pesticidal products waste water according to claim 1, it is characterised in that institute State step 4) in regulation pH value be 6.0-7.0.
7. the processing method of methoxy acrylic Pesticidal products waste water according to claim 1, it is characterised in that institute State step 4) in reaction equation it is as follows:
H2SO4+2KOH→K2SO4+2H2O
3KOH+FeCl3→Fe(OH)3↓+3KCl。
8. the processing method of methoxy acrylic Pesticidal products waste water according to claim 1, it is characterised in that institute State step 5) in flocculate include the small organic molecule that can flocculate of iron hydroxide and small part.
9. the processing method of methoxy acrylic Pesticidal products waste water according to claim 1, it is characterised in that institute State step 2) and step 3) in reaction generation gas and the step 6) in evaporation process produce gas through Alkali absorption process.
10. the processing method of methoxy acrylic Pesticidal products waste water according to claim 9, it is characterised in that The Alkali absorption is carried out using two-stage spray column, and the alkali in the Alkali absorption is sodium hydrate aqueous solution or aqueous sodium carbonate.
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CN109761423A (en) * 2019-01-24 2019-05-17 安徽广信农化股份有限公司 A kind of process for treating waste liquor synthesizing Fluoxastrobin
CN110921901A (en) * 2019-12-07 2020-03-27 衡水均凯化工有限公司 Treatment method of alkaline waste liquid
CN111499063A (en) * 2019-12-27 2020-08-07 利民化学有限责任公司 Comprehensive recycling treatment system and method for p-methylsulfonyl toluene wastewater

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