Method for treating casing processing wastewater and application of treatment product

A technology for processing wastewater and casings, applied in chemical instruments and methods, multi-stage water/sewage treatment, water/sludge/sewage treatment, etc. The problem of high oxygen content can reduce the difficulty of treatment, save resources and simplify the treatment method.

Inactive Publication Date: 2014-07-30
CHONGQING TIANSHI ANIMAL PROD
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Casing wastewater belongs to organic wastewater, which is rich in animal protein, fat and other organic substances that are difficult to degrade. It should not be discharged directly. The chemical oxygen consumption is also relatively high, ranging from 625 to 21000mg / L, while the content of inorganic nitrogen is very low. That is, the nutrient structure of the wastewater composition is extremely unreasonable, the wastewater is difficult to be treated by conventional methods, and there is a huge environmental risk in the direct discharge of high-concentration wastewater

Method used

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  • Method for treating casing processing wastewater and application of treatment product
  • Method for treating casing processing wastewater and application of treatment product
  • Method for treating casing processing wastewater and application of treatment product

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Embodiment 1

[0020] Embodiment 1: Unless otherwise specified below, the operating methods are all carried out at normal temperature and normal pressure.

[0021] A method for treating casing processing wastewater developed by the present invention comprises the following steps: (1) under the condition of temperature of 45-55°C, the pH value of the casing processing wastewater is adjusted to 6.0-7.0 with a mass concentration of 10% hydrochloric acid , to obtain solution I;

[0022] (2) Add chelating agent in the solution I obtained, and stir evenly, the time of stirring is 60~90min, obtains solution II;

[0023] (3) Add a coagulation aid to the obtained solution II, and stir evenly for 3 to 5 minutes to obtain a solution III;

[0024] (4) Add flocculant to the obtained solution III, and stir evenly for 1 to 3 minutes to obtain solution IV;

[0025] (5) The obtained solution IV was left to stand for 1 to 3 hours, and after collecting the supernatant, the precipitate was filtered, and the f...

Embodiment 2

[0040] Embodiment 2: Invention and development of a method for treating casing processing wastewater, comprising the following steps, (1) under the condition of a temperature of 45 to 55°C, the pH value of the casing processing wastewater is adjusted to 10% hydrochloric acid with a mass concentration of 6.0~7.0, to obtain solution I;

[0041] (2) Add chelating agent in the solution I obtained, and stir evenly, the time of stirring is 60~90min, obtains solution II;

[0042] (3) Add a coagulation aid to the obtained solution II, and stir evenly for 3 to 5 minutes to obtain a solution III;

[0043] (4) Add flocculant to the obtained solution III, and stir evenly for 1 to 3 minutes to obtain solution IV;

[0044] (5) The obtained solution IV was left to stand for 1 to 3 hours, and after collecting the supernatant, the precipitate was filtered, and the filtered precipitate contained amino acid chelates and protein peptides;

[0045] (6) drying the sediment obtained by filtration;...

Embodiment 3

[0054] Embodiment 3: Invention and development of a method for treating casing processing wastewater, comprising the following steps, (1) under the condition of a temperature of 45 to 55°C, the pH value of the casing processing wastewater is adjusted to 10% hydrochloric acid with a mass concentration of 6.0~7.0, to obtain solution I;

[0055] (2) Add chelating agent in the solution I obtained, and stir evenly, the time of stirring is 60~90min, obtains solution II;

[0056] (3) Add a coagulation aid to the obtained solution II, and stir evenly for 3 to 5 minutes to obtain a solution III;

[0057] (4) Add flocculant to the obtained solution III, and stir evenly for 1 to 3 minutes to obtain solution IV;

[0058] (5) The obtained solution IV was left to stand for 1 to 3 hours, and after collecting the supernatant, the precipitate was filtered, and the filtered precipitate contained amino acid chelates and protein peptides;

[0059] (6) drying the sediment obtained by filtration;...

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Abstract

The invention discloses a method for treating casing processing wastewater. The method comprises the following steps: (1) regulating the PH value of the casing processing wastewater to be 6.0-7.0 with hydrochloric acid with mass concentration of 10%, thus obtaining a solution I; (2) adding a chelating agent to the obtained solution I, thus obtaining a solution II; (3) adding a coagulant aid to the obtained solution II, thus obtaining a solution III; (4) adding a flocculant to the obtained solution III, thus obtaining a solution IV; (5) enabling the obtained solution IV to stand for 1-3 hours, collecting the supernatant, and then filtering the precipitate; (6) drying the filtered precipitate; (7) treating the collected supernatant with ultrafiltration and nanofiltration membranes. The method has the advantages that polypeptides and amino acids, which are not easy to extract, in the casing processing wastewater are extracted by synthesizing an amino acid chelate with the polypeptides and amino acids, so that the extraction ratio is high; the reclaimed water can be recycled, thus saving the resources; the treatment method is simple, is easy to control and simultaneously has economic and environmental benefits.

Description

Technical field [0001] The present invention is a technical field of water treatment in environmental engineering. It is specifically a method of processing the wastewater and the application of the processing products. Background technique [0002] my country is the big country of pig resources, the largest producer of the world's casing, and the main supply country of heparin raw materials.Due to the abundant small intestine resources, the heparin content in its mucosa is also high. At present, most of the domestic lated mucosal waste shaved in the process of gastropics is used as raw materials to extract heparin sodium.my country exports more than 100 tons of heparin and sodium sodium sodium each year. According to the estimation of the discharge of the wastewater in my country ’s casing processing, it is 2250 to 7500T / d, and the heparin processing wastewater is about 6000T / d.Including wastewater is an organic wastewater. It is rich in organic substances such as animal protein...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C02F9/04
Inventor 宁发子唐伏伦邓小玲辜玲
Owner CHONGQING TIANSHI ANIMAL PROD
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