Method for processing erythrocin film slurry by virtue of hydrothermal carbonization reaction

A technology of hydrothermal carbonization and erythromycin, which is applied in water/sewage treatment, natural water treatment, chemical instruments and methods, etc., can solve the problems of difficulty in meeting the effluent standards, difficulty in aerobic treatment, and labor and material resources, and shorten the The effect of processing cycle time, burden reduction, and processing cost reduction

Inactive Publication Date: 2018-11-27
NINGXIA PAGODA CHEM CENT LAB CO LTD
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0003] Erythromycin membrane slurry is erythromycin fermentation broth, in which the residual antibiotics and high-concentration organic matter are difficult to achieve the expected treatment effect by traditional biological treatment, because the strong inhibitory effect of residual antibiotics on microorganisms poisons aerobic bacteria, causing good Oxygen treatment is difficult; and anaerobic treatment of high-concentration organic matter is difficult to meet the effluent standard, and further treatment is required
The treatment of erythromycin membrane slurry using a single biochemical treatment cannot completely solve the problem, and necessary pretreatment must be carried out
The erythromycin membrane slurry pretreatment process consumes a lot of manpower and material resources due to the heavy load, long treatment cycle and high cost. Problems such as deodorization, antibiotic degradation and emission standards still need to be solved urgently

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0020] (1) To the erythromycin film slurry with a solid content of 70%, first add 5000ppm polyaluminum chloride, stir for 2 minutes, then place it for 10 minutes, add 500ppm polyacrylamide, stir for 1 minute, stand for 20 minutes, and filter under normal pressure to obtain a solid filter residue;

[0021] (2) Add (1+1) HNO to the solid filter residue 3 Mix, adjust pH<3, and form a suspension;

[0022] (3) Carry out hydrothermal carbonization reaction in the reactor, the carbonization temperature is 180℃, and the carbonization time is 8h;

[0023] (4) After carbonization, evaluate the carbonization effect, and treat the solid filter residue and liquid separately.

Embodiment 2

[0025] (1) To the erythromycin film slurry with a solid content of 50%, first add 1500ppm polyaluminum chloride, stir for 2 minutes, then place for 10 minutes, add 150ppm polyacrylamide, stir for 1 minute, stand for 20 minutes, and vacuum filter to obtain a solid filter residue;

[0026] (2) Add (1+1) HNO to the solid filter residue 3 Mix, adjust pH<3, and form a suspension;

[0027] (3) Carry out hydrothermal carbonization reaction in the reactor, the carbonization temperature is 220°C, and the carbonization time is 6h;

[0028] (4) After carbonization, evaluate the carbonization effect, and treat the solid dregs and liquid separately.

Embodiment 3

[0030] (1) To the erythromycin film slurry with a solid content of 40%, first add 900ppm polyaluminum chloride, stir for 2 minutes, then place it for 10 minutes, add 90ppm polyacrylamide, stir for 1 minute, stand for 20 minutes, and filter under normal pressure to obtain a solid filter residue;

[0031] (2) Add (1+1) HNO to the solid filter residue 3 Mix, adjust pH<3, and form a suspension;

[0032] (3) Carry out hydrothermal carbonization reaction in the reactor, the carbonization temperature is 200℃, and the carbonization time is 6h;

[0033] (4) After carbonization, evaluate the carbonization effect, and treat the solid medicinal residue and liquid separately.

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PUM

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Abstract

The invention provides a method for processing erythrocin film slurry by virtue of hydrothermal carbonization reaction. The method specifically comprises the steps of firstly carrying out solid-liquidseparation on the erythrocin film slurry through coagulation and flocculation so as to obtain filter residues, adding a certain amount of catalyst into the filter residues, adding two suspension solutions into a reaction kettle, carrying out hydrothermal carbonization reaction, and after the hydrothermal carbonization reaction is finished, filtering, so as to obtain filter residues and filtrate,wherein the filter residues can be used as a fuel or can be used for preparing activated carbon through modification, and the filtrate is continuously applied to a water treatment procedure. Accordingto the method provided by the invention, the processing period of the erythrocin film slurry is greatly shortened, the cost is saved, and the resource reutilization is realized; and the hydrothermalcarbonization reaction is simple, the foul smell of the erythrocin film slurry can be removed through the hydrothermal carbonization reaction, and antibiotics in the erythrocin film slurry can be degraded, so that the method is economic and practical and has wide market prospects.

Description

technical field [0001] The invention relates to the fields of pharmaceutical wastewater treatment and solid waste treatment, in particular to a method for treating erythromycin film slurry by hydrothermal carbonization reaction. Background technique [0002] Pharmaceutical wastewater mainly includes four categories: antibiotic production wastewater, synthetic drug production wastewater, Chinese patent medicine production wastewater, and washing water and flushing wastewater in the production process of various preparations. The wastewater is characterized by complex components, high organic content, high toxicity, deep color and high salt content, especially poor biochemical properties, and intermittent discharge, which is difficult to treat industrial wastewater. With the development of my country's pharmaceutical industry, pharmaceutical wastewater has gradually become one of the important sources of pollution. How to deal with this type of wastewater is a difficult proble...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C02F9/04C02F11/18C10B53/00C02F103/34
CPCC02F1/5236C02F1/56C02F1/66C02F11/18C02F2103/343C10B53/00
Inventor 张瑞杨惠琳刘晓燕
Owner NINGXIA PAGODA CHEM CENT LAB CO LTD
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