CN105152357B - A kind of pharmaceutical intermediate wastewater accelerant for biological treatment and preparation method and application - Google Patents

A kind of pharmaceutical intermediate wastewater accelerant for biological treatment and preparation method and application Download PDF

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CN105152357B
CN105152357B CN201510554987.6A CN201510554987A CN105152357B CN 105152357 B CN105152357 B CN 105152357B CN 201510554987 A CN201510554987 A CN 201510554987A CN 105152357 B CN105152357 B CN 105152357B
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biological treatment
accelerant
pharmaceutical intermediate
vitamin
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CN105152357A (en
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朱铿腾
杨金花
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HAIMEN HUANGHAI PIONEER PARK SERVICES CO., LTD.
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Quanzhou East Trading Co Ltd
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Abstract

The invention discloses a kind of pharmaceutical intermediate wastewater accelerant for biological treatment and preparation method and application, belong to field of waste water treatment.The accelerator is by glucose, ammonium phosphate, ethanol, phenol, calcium chloride, zinc chloride, magnesium sulfate, ferrous sulfate, vitamin B1, vitamin B12Compatibility is constituted, and is added it in pharmaceutical intermediate wastewater processing system, can promote the growth of microorganism, starts the Co metabolism effect of microorganism, resistance to poison of the microorganism to medicine intermediate is improved, so that the treatment pharmaceutical intermediate wastewater of efficient stable.The accelerator raw material sources extensively, prepare simple, easy to use, suitable pharmaceutical intermediate wastewater water quality characteristicses, have broad application prospects.

Description

A kind of pharmaceutical intermediate wastewater accelerant for biological treatment and preparation method and application
Technical field
The present invention relates to the preparation and application of a kind of accelerant for biological treatment, more particularly to a kind of life of pharmaceutical intermediate wastewater Thing treatment accelerator and preparation method and application, belongs to field of industrial waste water treatment, belongs to biological reinforcing technology category.
Background technology
Medicine intermediate production belongs to fine chemistry industry industry, mainly using the method for chemical reactive synthesis, by organic matter Matter and inorganic substances are made synthetic drug and pharmaceutical intermediate.The main production of medicine intermediate is all chemical reaction, its Because reactions steps are more in production process, using various chemical raw materials, production process raw material availability is low, and product yield is low, stream Lose seriously, therefore contain miscellaneous toxic and harmful substance, such as amino benzenes compounds, nitro class chemical combination in this kind of waste water Thing, arene compounds, halogenated hydrocarbon compound, organic solvent such as toluene, chloroform, petroleum ether, ethyl acetate, acetone etc., with And the multiple pollutant such as spent acid alkali, inorganic salts.Therefore, pharmaceutical intermediate wastewater is the big industry of universally acknowledged difficulty of governance One of waste water, it is difficult to which treatment up to standard is carried out to it using conventional bioremediation.
Biological reinforcing technology is by adding nutriment, five poisonous creatures: scorpion, viper, centipede, house lizard, toad surfactant, electron acceptor in contaminated environment Or co-metabolic substance, the microorganism with degradation of contaminant ability itself existed in activation contaminated environment, make its active To greatly improving, fast-growth is bred, so as to remove pollutant.Microorganism Co metabolism as biological reinforcing technology important hand Section, is particularly suited for being difficult in biodegradable Industrial Wastewater Treatment, and co-metabolic substance is added in industrial wastewater, can promote The growth of microorganism, starts the Co metabolism effect of microorganism, improves resistance to poison of the microorganism to organic pollution, and microorganism is in profit While with these matrix, common oxidation or other reactions can occur to target contaminant, and excite rest cell to mesh The metabolism of pollutant is marked, so that hardly degraded organic substance is able to degraded removal in industrial wastewater.
The content of the invention
It is big to pharmaceutical intermediate wastewater intractability in order to overcome the shortcomings of conventional biological treatment method, it is of the invention by biology Microorganism Co metabolism is acted on and organically combined with conventional biological treatment method, i.e., add biological treatment in conventional biological treatment system Accelerator, reaches the growth for promoting microorganism, the Co metabolism effect for starting microorganism, improves microorganism to the resistance to of organic pollution The purpose of toxicity, rapid degradable organic pollutant.
In order to achieve the above object, the technical scheme is that, one:A kind of pharmaceutical intermediate wastewater biological treatment promotees Enter agent;Secondly:The preparation method of the accelerant for biological treatment;Thirdly:The accelerant for biological treatment is at pharmaceutical intermediate wastewater Application in reason.
One:A kind of pharmaceutical intermediate wastewater accelerant for biological treatment, is made up of following blend components and weight portion:
Glucose:30-60 parts;
Ammonium phosphate:10-20 parts;
Ethanol:10-20 parts;
Phenol:1-5 parts;
Calcium chloride:1-5 parts;
Zinc chloride:1-5 parts;
Magnesium sulfate:0.2-1 parts;
Ferrous sulfate:0.2-1 parts;
Vitamin B1:0.1-0.5 parts;
Vitamin B12:0.1-0.3 parts;
Water:200-300 parts.
Preferably, the accelerator is made up of following blend components and weight portion:
Glucose:40-50 parts;
Ammonium phosphate:12-15 parts;
Ethanol:15-18 parts;
Phenol:2-4 parts;
Calcium chloride:2-3 parts;
Zinc chloride:1-2 parts;
Magnesium sulfate:0.5-0.8 parts;
Ferrous sulfate:0.3-0.6 parts;
Vitamin B1:0.2-0.3 parts;
Vitamin B12:0.1-0.2 parts;
Water:250-300 parts.
It is furthermore preferred that the accelerator is made up of following blend components and weight portion:
Glucose:45 parts;
Ammonium phosphate:15 parts;
Ethanol:18 parts;
Phenol:3 parts;
Calcium chloride:2 parts;
Zinc chloride:1 part;
Magnesium sulfate:0.8 part;
Ferrous sulfate:0.4 part;
Vitamin B1:0.25 part;
Vitamin B12:0.15 part;
Water:280 parts.
Secondly:The preparation method of above-mentioned accelerant for biological treatment comprises the following steps:
(1) dissolve:The phenol and ethanol of weight portion are weighed, phenol is dissolved in ethanol, stirring accelerates its dissolving to obtain Solution is 1.;Weigh glucose, ammonium phosphate, calcium chloride, zinc chloride, magnesium sulfate, ferrous sulfate, the vitamin B of weight portion1, dimension life Plain B2, above-mentioned substance is dissolved in the water of weight portion, stirring accelerates its dissolving, obtains solution 2.;
(2) mix:1. solution is added to solution 2. in, stir 1-2 hour, make it well mixed, that is, in obtaining medicine Mesosome biological wastewater treatment accelerator.
(3) store:The accelerant for biological treatment of preparation is kept in dark place, it is standby, for the treatment of pharmaceutical intermediate wastewater.
Thirdly:Application process of the above-mentioned accelerant for biological treatment in pharmaceutical intermediate wastewater treatment is as follows:
To be used after accelerant for biological treatment dilute with water, it is preferred that extension rate is 10 times;
Accelerant for biological treatment after dilution is added to the water inlet in biological treatment system;Preferably, at biology Reason system is any of the conventional biological treatment techniques such as cyclic activated sludge system, SBR techniques, A/O techniques, AB techniques, contact oxidation technology It is a kind of.
Accelerant for biological treatment after dilution adds ratio for 50-100mg/g (CODcr)。
Advantageous Effects of the invention are as follows:
1) raw material of the present invention is cheap and easy to get, scientific and reasonable according to pharmaceutical intermediate wastewater water quality compatibility, has microorganism life concurrently Matrix long, energy matter, trace element and growth factor.Wherein glucose, ethanol and phenol are used as growth substrate, biological utilisation Rate is high, enhances carbon source synergistic metabolism effect;Ammonium phosphate also provides nitrogen source and phosphorus source as energy matter, optimizes carbon N/P ratio, Promote growth of microorganism;Calcium chloride, zinc chloride, magnesium sulfate and ferrous sulfate are strengthened to microorganism key enzyme as trace element Induction and energy supply, be conducive to exciting rest cell to the degradation capability of target contaminant;Vitamin B1, vitamin B12Make It is growth factor, promotes microbial growth, accelerates the foundation of Co metabolism system.The accelerator of above compatibility can effectively excite Microorganism Co metabolism is acted on, metabolism of the enhancement microbiological to target contaminant.
6) preparation process is simple, is easy to storage, convenient and swift using process.Only need in conventional biological treatment system Accelerator after the simple dosing dilution of water inlet, does not introduce other units and processing equipment, without any several inputs, should With extensive, can be adapted to improve the reinforcing of existing sewage treatment facility efficiency using manually adding, without increasing energy consumption.
7) effect of biological micro-organism Co metabolism and conventional biological treatment method are organically combined, overcomes conventional biological treatment The method deficiency big to pharmaceutical intermediate wastewater intractability, promotes the growth of microorganism, starts the Co metabolism effect of microorganism, Microorganism is improved to the resistance to poison of organic pollution, the clearance of COD in waste water is not only greatly improved, and it is useless to degrade rapidly Phenyl amines, aromatic hydrocarbons, halogenated hydrocarbon and various organic solvents in water.
8) treatment effect stabilization, processing cost is cheap, and the accelerant for biological treatment after 10 times of dilution adds ratio for 50- 100mg/g(CODcr).Pharmaceutical intermediate wastewater after treatment, COD, ammonia nitrogen removal frank more than 95%, aniline, halo The persistence organic pollutant such as hydrocarbon clearance is respectively 80% and more than 85%.Waste water treatment efficiency is high, simple possible, is easy to work Industryization is implemented.
Specific embodiment
Hereinafter the present invention will be further illustrated by specific embodiment, it will be understood by those skilled in the art that of the invention Specific embodiment limits the present invention never in any form.Any equivalent each falls within guarantor of the invention on the basis of the present invention Within the scope of shield.
Embodiment 1:
The preparation of pharmaceutical intermediate wastewater accelerant for biological treatment
Phenol 3kg is weighed, is dissolved in 18kg ethanol, stirring accelerates its dissolving to obtain solution 1.;Weigh glucose 45kg, Ammonium phosphate 15kg, calcium chloride 2kg, zinc chloride 1kg, magnesium sulfate 0.8kg, ferrous sulfate 0.4kg, vitamin B10.25kg, dimension life Plain B120.15kg, above-mentioned substance is dissolved in 280kg water, and stirring accelerates its dissolving, obtains solution 2.;1. solution is added To solution 2. in, stir 1-2 hour, make it well mixed, that is, obtain pharmaceutical intermediate wastewater accelerant for biological treatment.
Embodiment 2:
The preparation of pharmaceutical intermediate wastewater accelerant for biological treatment
Phenol 2kg is weighed, is dissolved in 17kg ethanol, stirring accelerates its dissolving to obtain solution 1.;Weigh glucose 50kg, Ammonium phosphate 12kg, calcium chloride 3kg, zinc chloride 2kg, magnesium sulfate 0.6kg, ferrous sulfate 0.5kg, vitamin B10.2kg, dimension life Plain B120.2kg, by above-mentioned substance dissolving 300kg water, stirring accelerates its dissolving, obtains solution 2.;1. solution is added to molten Liquid 2. in, stir 1-2 hour, make it well mixed, that is, obtain pharmaceutical intermediate wastewater accelerant for biological treatment.
Embodiment 3:
The preparation of pharmaceutical intermediate wastewater accelerant for biological treatment
Phenol 5kg is weighed, is dissolved in 18kg ethanol, stirring accelerates its dissolving to obtain solution 1.;Weigh glucose 40, phosphorus Sour ammonium 18kg, calcium chloride 5kg, zinc chloride 2kg, magnesium sulfate 0.3kg, ferrous sulfate 0.5kg, vitamin B10.5kg, vitamin B120.2kg, above-mentioned substance is dissolved in 260kg water, and stirring accelerates its dissolving, obtains solution 2.;1. solution is added to molten Liquid 2. in, stir 1-2 hour, make it well mixed, that is, obtain pharmaceutical intermediate wastewater accelerant for biological treatment.
Embodiment 4:
The application of pharmaceutical intermediate wastewater accelerant for biological treatment
Certain pharmacy corporation mainly produces the medicine intermediates, its sewage disposal system such as cephalosporanic acid class, the southern class of training, miazines Using cyclic activated sludge system as the aerobic stage of sewage disposal, after accelerant for biological treatment prepared by embodiment 1 dilutes 10 times, throw The water inlet in CASS ponds is added to, ratio is added for 80mg/g (CODcr).Detection Inlet and outlet water water quality index, is shown in Table one.
Table one:Water quality index result list
As shown in Table 1:In with the system of cyclic activated sludge system treatment pharmaceutical intermediate wastewater, biological treatment of the present invention is being added During accelerator, CODCr、NH3- N, aniline, the clearance of halogenated hydrocarbons are respectively 96.1%, 95.1%, 80.8%, 88.8%;And When not adding accelerant for biological treatment of the present invention, CODCr、NH3- N, aniline, the clearance of halogenated hydrocarbons be respectively 87.5%, 74.6%th, 62.2%, 68.6%;After adding accelerant for biological treatment of the present invention in conventional cyclic activated sludge system, COD, ammonia nitrogen, benzene Amine, the clearance of halogenated hydrocarbons are respectively increased 9.8%, 27.5%, 29.9% and 29.4%, and bioaugmentation is obvious.
Embodiment 5:
The Comparison study experiment of pharmaceutical intermediate wastewater accelerant for biological treatment
Experimental group:Accelerant for biological treatment prepared by embodiment 2.
Control group one:Accelerant for biological treatment prepared by embodiment 2 is made into following formula to change:Weigh glucose 50kg, Ammonium phosphate 22kg, ethanol 17kg, zinc chloride 2kg, magnesium sulfate 0.6kg, ferrous sulfate 0.5kg, vitamin B120.2kg, will be above-mentioned In material dissolving 300kg water, stirring accelerates its dissolving, stirs 1-2 hours, is well mixed it, obtains at the biology of control group one Reason accelerator.
Control group two:Dyeing and Printing Wastewater Biological Treatment accelerator prepared by embodiment 2 is made following formula and is changed:Weigh phenol 6kg, is dissolved in 25kg ethanol, and stirring accelerates its dissolving to obtain solution 1.;Weigh glucose 25kg, ammonium phosphate 12kg, chlorination Calcium 7kg, zinc chloride 0.8kg, magnesium sulfate 1.5kg, ferrous sulfate 0.1kg, vitamin B11kg, vitamin B120.06kg, will be upper State in material dissolving 300kg water, stirring accelerates its dissolving, obtains solution 2.;1. solution is added to solution 2. in, stir 1-2 Hour, be well mixed it, that is, obtain the accelerant for biological treatment of control group two.
Blank group:Accelerant for biological treatment is not added
Contrast treatment is carried out to certain pharmaceutical intermediate wastewater in laboratory day treatment wastewater flow rate is for the sbr reactor device of 200L Experiment.After the experimental group of above-mentioned preparation, control group one, the accelerant for biological treatment of control group two are diluted into 10 times, add respectively To the water inlet of contact-oxidation pool, the ratio of adding is 100mg/g (CODcr).Detection Inlet and outlet water water quality index, is shown in Table two.
Table two:Water quality index comparing result list
As shown in Table 2:In with the system of contact oxidation technology treatment pharmaceutical intermediate wastewater, biology of the invention is being added During treatment accelerator, CODCr、NH3- N, aniline, the clearance of halogenated hydrocarbons are respectively 95.9%, 95.2%, 81.3%, 88.5%; (remove phenol, calcium chloride, the vitamin B in formula when the accelerant for biological treatment of control group one is added1), CODCr、NH3- N, aniline, the clearance of halogenated hydrocarbons are respectively 87.9%, 77.1%, 65.3%, 70.5%;At the biology for adding control group two (weight portion of each component is not in ratio range of the present invention in formula), COD during reason acceleratorCr、NH3- N, aniline, halogenated hydrocarbons Clearance is respectively 86.9%, 70.2%, 59.5%, 62.1%;When accelerant for biological treatment of the present invention is not added, CODCr、 NH3- N, aniline, the clearance of halogenated hydrocarbons are respectively 87.2%, 72.6%, 69.9%, 75.8%.It can be seen that, it is each in control group one The clearance of polluter is significantly lower than experimental group, and suitable with blank group, and microorganism is not excited in this explanation control group one Co metabolism effect.The clearance of each polluter is significantly lower than experimental group, even below blank group, this explanation in control group two Because proportioning exceeds ratio range of the present invention in control group two, do not excite not only the Co metabolism of microorganism to act on, instead result in The disorder of processing system.Therefore, the compatibility composition and weight of accelerant for biological treatment of the present invention can not arbitrarily change, Change compatibility composition and beyond ratio range, can not effectively process pharmaceutical intermediate wastewater.

Claims (9)

1. a kind of pharmaceutical intermediate wastewater accelerant for biological treatment, it is characterised in that be made up of following blend components, each component and Its weight portion is constituted:
Glucose:40-50 parts;
Ammonium phosphate:12-15 parts;
Ethanol:15-18 parts;
Phenol:2-4 parts;
Calcium chloride:2-3 parts;
Zinc chloride:1-2 parts;
Magnesium sulfate:0.5-0.8 parts;
Ferrous sulfate:0.3-0.6 parts;
Vitamin B1:0.2-0.3 parts;
Vitamin B12:0.1-0.2 parts;
Water:250-300 parts.
2. pharmaceutical intermediate wastewater accelerant for biological treatment as claimed in claim 1, it is characterised in that by following blend components Composition, each component and its weight portion composition are:
Glucose:45 parts;
Ammonium phosphate:15 parts;
Ethanol:18 parts;
Phenol:3 parts;
Calcium chloride:2 parts;
Zinc chloride:1 part;
Magnesium sulfate:0.8 part;
Ferrous sulfate:0.4 part;
Vitamin B1:0.25 part;
Vitamin B12:0.15 part;
Water:280 parts.
3. the preparation method of the pharmaceutical intermediate wastewater accelerant for biological treatment as described in claim 1-2 is any, its feature exists In comprising the following steps:
(1) dissolve:The phenol and ethanol of weight portion are weighed, phenol is dissolved in ethanol, stirring accelerates its dissolving to obtain solution ①;Weigh glucose, ammonium phosphate, calcium chloride, zinc chloride, magnesium sulfate, ferrous sulfate, the vitamin B of weight portion1, vitamin B12, Above-mentioned substance is dissolved in the water of weight portion, stirring accelerates its dissolving, obtains solution 2.;
(2) mix:1. solution is added to solution 2. in, stir 1-2 hour, make it well mixed, that is, obtain medicine intermediate Biological wastewater treatment accelerator;
(3) store:The accelerant for biological treatment of preparation is kept in dark place, it is standby, for the treatment of pharmaceutical intermediate wastewater.
4. the pharmaceutical intermediate wastewater accelerant for biological treatment as described in claim 1-2 is any is in pharmaceutical intermediate wastewater treatment In application.
5. application as claimed in claim 4, it is characterised in that will be used after accelerant for biological treatment dilute with water.
6. application as claimed in claim 5, it is characterised in that extension rate is 10 times.
7. application as claimed in claim 6, it is characterised in that the accelerant for biological treatment after dilution is added to biological treatment Water inlet in system.
8. application as claimed in claim 7, it is characterised in that add ratio for 50-100mg/g (CODcr)。
9. application as claimed in claim 8, it is characterised in that the biological treatment system is cyclic activated sludge system, SBR techniques, A/O Any one in technique, AB techniques, contact oxidation technology.
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CN109626550A (en) * 2018-12-29 2019-04-16 凯瑞斯德生化(苏州)有限公司 The application of 5,6- dihydro -4- hydroxyl -6- methylthiophene [2,3-b] sulphur pyrans -7,7- dioxide
CN113461150B (en) * 2021-07-28 2022-03-11 湖北亮绿环保技术有限公司 Treatment process of medical intermediate chemical wastewater
CN113998789A (en) * 2021-10-29 2022-02-01 中原环保股份有限公司 COD for domestic sewage treatmentCrBiological removal promoter and preparation method thereof
CN115231716B (en) * 2022-08-02 2024-05-10 河南君和环保科技有限公司 Biological promoter for treating wastewater produced by ion exchange resin, and preparation method and application thereof

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Publication number Priority date Publication date Assignee Title
WO2012079140A1 (en) * 2010-12-14 2012-06-21 Gustavo Casal De Rey Biostimulation and bioenhancing processes for treating domestic and industrial effluents
CN103848504A (en) * 2012-11-28 2014-06-11 沈阳铝镁设计研究院有限公司 Biological enhancer, its preparation method and application method thereof
CN104711213A (en) * 2015-03-13 2015-06-17 中国海洋石油总公司 Accelerant facilitating growth of salt-resistive nitrifying bacteria in high-salt wastewater

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2012079140A1 (en) * 2010-12-14 2012-06-21 Gustavo Casal De Rey Biostimulation and bioenhancing processes for treating domestic and industrial effluents
CN103848504A (en) * 2012-11-28 2014-06-11 沈阳铝镁设计研究院有限公司 Biological enhancer, its preparation method and application method thereof
CN104711213A (en) * 2015-03-13 2015-06-17 中国海洋石油总公司 Accelerant facilitating growth of salt-resistive nitrifying bacteria in high-salt wastewater

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