Method for multistage anaerobic treatment of etimicin sulfate production wastewater

A technology for etimicin sulfate and production wastewater, which is applied in anaerobic digestion treatment, water/sewage multi-stage treatment, multi-stage water treatment, etc. Lack of problems such as reducing COD and residual antibiotics, reducing emissions and environmental risks, and reducing the use of pumps

Inactive Publication Date: 2019-01-18
CHANGZHOU FANGYUAN PHARMA +3
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  • Abstract
  • Description
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Problems solved by technology

[0002] Etimicin sulfate is an aminoglycoside antibiotic commonly used clinically, mainly composed of gentamicin C 1a It is obtained after chemical synthesis, and a large amount of synthetic wastewater is produced in the production process, and a part of gentamicin C remains in the wastewater 1a , while gentamicin C 1a It has a strong inhibitory effect on both Gram-positive bacteria and negative bacteria. If the high-concentration wastewater is directly anaerobically treated, the COD removal effect is often poor, resulting in high COD in the effluent
At the same time, due to the lack of nutrients in chemically synthesized wastewater, the efficiency of biological treatment for chemically synthesized wastewater is usually low
[0003] Chinese patent CN 104986853A, a method for treating spiramycin fermentation wastewate

Method used

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  • Method for multistage anaerobic treatment of etimicin sulfate production wastewater

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Embodiment 1

[0027] Embodiment 1: as figure 1 As shown, the treatment equipment of the present invention is made of hydrolytic acidification tank, 3 anaerobic reactors and 1 intermediate water tank, and intermediate water tank is positioned between the first-stage anaerobic reactor and the second-stage anaerobic reactor, and the second-stage Between the anaerobic reactor and the third-stage anaerobic reactor, water flows by gravity.

[0028] Pump high-concentration etimicin sulfate chemically synthesized wastewater (COD is 16230mg / L, gentamicin C1a content is 32.2mg / L) into the hydrolytic acidification tank with a volume of 0.5m 3 , the inflow flow is 0.1m 3 / h, adjust the oxidation-reduction potential in the hydrolytic acidification pool to -100~50mV, and control the pH in the hydrolytic acidification pool to 6.5±0.2.

[0029] Pump the effluent from the hydrolytic acidification tank into the first-stage anaerobic reactor with a flow rate of 0.15m 3 / h, the effective volume of the first...

Embodiment 2

[0032] Embodiment 2: as figure 1 As shown, the treatment equipment consists of a hydrolytic acidification tank, a first-stage anaerobic reactor, an intermediate water tank, and a second-stage anaerobic reactor in series.

[0033] Pump high-concentration etimicin sulfate chemically synthesized wastewater (COD is 15294mg / L, gentamicin C1a content is 30.7mg / L) into the hydrolytic acidification tank with a volume of 250m 3 , the inflow flow rate is 42m 3 / h, adjust the oxidation-reduction potential in the hydrolytic acidification pool to -80~50mV, and control the pH in the hydrolytic acidification pool to 6.5±0.2.

[0034] Pump the effluent from the hydrolytic acidification tank into the first-stage anaerobic reactor with a flow rate of 63m3 / h, and the effective volume of the first-stage anaerobic reactor is 3.75m 3 . The effluent treated by the first-stage anaerobic reactor overflows into the intermediate water tank, and NaOH is added to the intermediate water tank to control ...

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Abstract

The invention discloses a method for multistage anaerobic treatment, which belongs to the field of wastewater treatment and aims to provide a treatment method for the production wastewater of etimicinsulfate, which effectively improves the treatment efficiency. The method is characterized in that the method comprises the following steps: step 1, the wastewater from etimicin sulfate production enters a hydrolysis acidification tank for acidification; step 2, effluent of the hydrolysis acidification tank enters a first stage anaerobic reactor; step 3, the effluent of the first stage anaerobic reactor overflows into an intermediate tank for the pH value adjustment; step 4, the effluent of the intermediate tank is divided into two parts, the first part flows into a multistage anaerobic reactor, and the overflow water from the top of the multistage reactor is the final effluent, the second part flows back to the hydrolysis acidification tank and is mixed with the etimicin sulfate production wastewater; operations of steps 1 to 4 are repeated. By adopting a hydrolytic acidification coupled tandem anaerobic reflow process according to the invention, an anaerobic biological treatment is performed on the etimicin sulfate wastewater, thereby greatly reducing COD and residual antibiotics in the wastewater.

Description

technical field [0001] The invention relates to the field of waste water treatment, in particular to a method for multistage anaerobic treatment of waste water produced by etimicin sulfate. Background technique [0002] Etimicin sulfate is an aminoglycoside antibiotic commonly used clinically, mainly composed of gentamicin C 1a It is obtained after chemical synthesis, and a large amount of synthetic wastewater is produced in the production process, and a part of gentamicin C remains in the wastewater 1a , while gentamicin C 1a It has a strong inhibitory effect on both Gram-positive bacteria and negative bacteria. If the high-concentration wastewater is directly anaerobically treated, the COD removal effect is often poor, resulting in high COD in the effluent. At the same time, due to the lack of nutrients in chemically synthesized wastewater, the efficiency of biological treatment for chemically synthesized wastewater is usually low. [0003] Chinese patent CN 104986853A,...

Claims

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Application Information

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IPC IPC(8): C02F9/14C02F3/28C02F101/38C02F103/34
CPCC02F1/66C02F3/286C02F2101/38C02F2103/343C02F2301/043C02F2301/08
Inventor 陈代杰胡东辉刘鹏宇李兴刚陈舟舟戴俊
Owner CHANGZHOU FANGYUAN PHARMA
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