Method for pretreating wastewater obtained from antibiotic production

A technology for antibiotic wastewater and production wastewater, which is applied in natural water treatment, water/sewage treatment, water treatment parameter control, etc. It can solve the problems of severe and harsh treatment conditions, low antibiotic residues, and reduce the biological toxicity of antibiotic production wastewater.

Active Publication Date: 2017-07-28
RES CENT FOR ECO ENVIRONMENTAL SCI THE CHINESE ACAD OF SCI
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

[0006] The purpose of the present invention is to provide a kind of pretreatment of fermented antibiotic production wastewater in order to solve the technical problem that the treatment conditions in the existing antibiotic production wastewater treatment process are severe and harsh, and the reaction can only be carried out under high temperature, strong acid or strong alkaline conditions. Method, the method of the present invention adopt

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  • Method for pretreating wastewater obtained from antibiotic production
  • Method for pretreating wastewater obtained from antibiotic production
  • Method for pretreating wastewater obtained from antibiotic production

Examples

Experimental program
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Effect test

Embodiment 1

[0099] The treatment of embodiment 1 streptomycin simulated wastewater

[0100] 1. Preparation of streptomycin simulated wastewater

[0101] Streptomycin sulfate standard substance was dissolved in ultrapure water to prepare streptomycin simulated wastewater solution, wherein the concentration of streptomycin sulfate in the streptomycin simulated wastewater solution was 100mg / L.

[0102] In the embodiment of the present invention, 50 mg of streptomycin sulfate standard substance was dissolved in 500 mL of ultrapure water to make streptomycin simulated waste water for subsequent use.

[0103] 2. Preparation of solid base catalyst (CaO-MgO composite metal oxide)

[0104] 2-1) Mix calcium acetate with ultrapure water, stir and dissolve evenly, and prepare an aqueous solution of calcium acetate, wherein the ratio of the mass of calcium acetate to the volume of ultrapure water is 7.36:100, that is, dissolve in 100ml of ultrapure water 7.36 g calcium acetate.

[0105] In the embo...

Embodiment 1A

[0124] The treatment of embodiment 1A streptomycin simulated wastewater

[0125] 1. Preparation of streptomycin simulated wastewater

[0126] Same as Example 1.

[0127] 2. Preparation of solid base catalyst (CaO-MgO composite metal oxide)

[0128] 2-1) Mix calcium acetate with ultrapure water, stir and dissolve evenly, and prepare an aqueous solution of calcium acetate, wherein the ratio of the mass of calcium acetate to the volume of ultrapure water is 2.78:100, that is, dissolve in 100ml of ultrapure water 2.78 g calcium acetate.

[0129] In the embodiment of the present invention, 2.78g of calcium acetate was dissolved in 100mL of ultrapure water to prepare an aqueous solution of calcium acetate for subsequent use.

[0130] 2-2) Weigh light MgO (10g) calcined at 500°C for 8 hours, place it in an aqueous solution of calcium acetate, and carry out impregnation treatment at a stirring rate of 300rpm, and stop stirring after impregnating for 6 hours, wherein the mass of MgO...

Embodiment 1B

[0139] The treatment of embodiment 1B streptomycin simulated wastewater

[0140] 1. Preparation of streptomycin simulated wastewater

[0141] Same as Example 1.

[0142] 2. Preparation of solid base catalyst (CaO-MgO composite metal oxide)

[0143] 2-1) Mix calcium acetate with ultrapure water, stir and dissolve evenly, and prepare an aqueous solution of calcium acetate, wherein the ratio of the mass of calcium acetate to the volume of ultrapure water is 7.9:100, that is, dissolve in 100ml of ultrapure water 7.9 g calcium acetate.

[0144] In the embodiment of the present invention, 7.9g of calcium acetate was dissolved in 100mL of ultrapure water to prepare an aqueous solution of calcium acetate for subsequent use.

[0145] 2-2) Weigh light MgO (10g) calcined at 500°C for 8 hours, place it in an aqueous solution of calcium acetate, and carry out impregnation treatment at a stirring rate of 300rpm, and stop stirring after impregnating for 6 hours, wherein the mass of MgO is...

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Abstract

The invention discloses a method for pretreating wastewater obtained from antibiotic production. The method comprises the following steps: adding a solid base to wastewater obtained from antibiotic production, and hydrolyzing the residual antibiotics in the wastewater obtained from antibiotic production under the action of the solid base. The method provided by the invention has high antibiotic degradation efficiency and low antibiotic residue, and the biological toxicity of the wastewater obtained from antibiotic production is significantly reduced. The antibiotic wastewater pretreated by the method provided by the invention can be directly subjected to the subsequent biochemical treatment. The method provided by the invention can completely remove the antibiotics in the antibiotic wastewater, reduce the inhibition of the high concentration antibiotics to microorganisms, reduce the difficulty of the subsequent biochemical treatment of the antibiotic wastewater, and reduce the production of drug-resistant bacteria and drug-resistant genes in the subsequent biochemical treatment.

Description

technical field [0001] The invention relates to a method for harmless treatment of waste in the pharmaceutical industry, in particular to a method for harmless treatment of waste liquid after producing antibiotics through fermentation, and belongs to the field of liquid waste treatment. Background technique [0002] Antibiotic pharmaceutical production wastewater is mainly high-concentration organic wastewater produced in the separation, extraction, refining and purification sections, such as crystallization liquid, waste mother liquor, etc., as well as washing wastewater from seed tanks, fermentation tanks, and cooling water from fermentation tanks. High-concentration organic wastewater with high pollution load, high toxicity, and strong antibacterial properties mainly comes from waste fermentation liquid or synthetic waste liquid after raw material extraction in the antibiotic production process. This type of wastewater, especially fermented antibiotic pharmaceutical waste...

Claims

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Application Information

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IPC IPC(8): C02F1/58C02F103/34C02F101/38C02F101/34
CPCC02F1/58C02F2209/44C02F2209/02C02F2103/343C02F2101/34C02F2101/38C02F2101/40Y02W10/10
Inventor 张昱唐妹杨敏高迎新田哲
Owner RES CENT FOR ECO ENVIRONMENTAL SCI THE CHINESE ACAD OF SCI
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