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Method for pretreating residual activated sludge of refinery plant by using alkaline residues

A residual activity, pretreatment technology, applied in sludge treatment, biological sludge treatment, chemical instruments and methods, etc., can solve the problems of limiting the application of sludge pretreatment technology, high equipment investment, operating costs and reagent costs, etc. To achieve the effect of collaborative processing, improve processing effect and reduce pretreatment cost

Pending Publication Date: 2021-11-23
CHINA UNIV OF PETROLEUM (BEIJING) +1
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  • Abstract
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  • Claims
  • Application Information

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Problems solved by technology

[0004] The above-mentioned residual activated sludge pretreatment technologies can effectively disintegrate the sludge floc structure and improve the efficiency of anaerobic digestion. However, high equipment investment, operating costs and reagent costs limit the application of sludge pretreatment technologies. Therefore, we are constantly looking for A suitable pretreatment method to improve the treatment effect of anaerobic digestion of excess activated sludge and reduce the cost of pretreatment of excess activated sludge is a research direction that researchers continue to pay attention to.

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  • Method for pretreating residual activated sludge of refinery plant by using alkaline residues
  • Method for pretreating residual activated sludge of refinery plant by using alkaline residues
  • Method for pretreating residual activated sludge of refinery plant by using alkaline residues

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Embodiment 1

[0036] The processing method of the refinery surplus activated sludge provided by the present embodiment comprises the following steps:

[0037] Step 1. Send the surplus activated sludge from the refinery into the secondary settling tank for natural sedimentation and concentration. The water content of the concentrated refinery surplus activated sludge is 95.8%, and the SCOD concentration in the supernatant is 87.5mg / L. Sludge VS is 18550mg / L;

[0038] Step 2, the pH value of the residual activated sludge of the refinery after measuring concentration is 7.5, each gets the residual activated sludge of the refinery after 1L of concentration, adds the NaOH solution of alkali slag (pH value is 13.5) and 3mol / L respectively to make The pH value of the mixed system of the concentrated refinery residual activated sludge and lye is 12, and it is stirred at room temperature at a speed of 300 rpm for 1 hour, and a blank group is set at the same time, that is, the concentrated refinery a...

Embodiment 2

[0045] This example mainly explores the influence of the dosage of alkali slag and pretreatment time on anaerobic digestion during the pretreatment process, and optimizes the pretreatment conditions of alkali slag:

[0046] Step 1. Send the surplus activated sludge from the refinery to the secondary settling tank for natural sedimentation and concentration. The water content of the concentrated refinery surplus activated sludge is 95.8%, the VS is 18550mg / L, and the COD concentration in the supernatant is 87.5mg / L;

[0047] Step 2, the pH value of the residual activated sludge of the refinery after measuring the concentration is 7.5, respectively get the residual activated sludge of the refinery after 1L of concentration, add alkali slag 10, 10, 20, 30, 40 and 50mL, stir quickly and evenly, and measure the pH values ​​of the mixed system of the refinery residual activated sludge and alkali slag after concentration in each group are: 10.0, 11.1, 12.1, 12.5 and 12.7, without adj...

Embodiment 3

[0054] This embodiment provides mainly to explore the impact of temperature on anaerobic digestion in the pretreatment process:

[0055] Step 1. Send the surplus activated sludge from the refinery into the secondary settling tank for natural sedimentation and concentration. The water content of the concentrated refinery surplus activated sludge is 95.6%, and the COD concentration in the supernatant is 88.3mg / L;

[0056] Step 2. Measure the pH value of the remaining activated sludge in the refinery to 7.2, take 1L of the remaining activated sludge in the refinery, add 30mL of alkali residue and stir quickly, and measure the concentrated activated sludge and alkali residue in the refinery The pH value of the mixed system is 12.3, and the mixed system is placed in a water bath at 80°C, and stirred at a speed of 300rpm for 2h with a stirrer;

[0057] Step 3, using 1 mol / L hydrochloric acid solution to adjust the pH value to the range of 7-7.5 to terminate the pretreatment reaction...

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Abstract

The invention provides a method for pretreating residual activated sludge of a refinery plant by using alkaline residues, which comprises the following steps of: (1) concentrating the residual activated sludge of the refinery plant, and carrying out mixing pretreatment on the concentrated residual activated sludge and alkaline residues discharged from the refinery plant to obtain pretreated residual activated sludge; (2) adjusting the pH value of the pretreated residual activated sludge until the sludge is neutral, and then carrying out anaerobic digestion treatment to obtain biogas and digestion residues; and (3) centrifuging the digestion residues, collecting solids, then carrying out landfill treatment, mixing supernate with the alkaline residues, and then carrying out alkaline residue biochemical treatment. According to the invention, a method of treating waste with waste is adopted, so that the treatment effect of anaerobic digestion of the residual activated sludge is improved, the pretreatment cost of the residual activated sludge is reduced, the amount of alkaline residues needing to be treated is reduced, cooperative treatment of the residual activated sludge of the refinery plant and the alkaline residues of the refinery plant is realized, and a new thought is provided for recycling, reducing and innocent treatment of refinery wastes.

Description

technical field [0001] The invention relates to a method for pretreating excess activated sludge in a refinery with alkali slag, and relates to the technical field of sludge treatment. Background technique [0002] With the continuous development of the petroleum industry, the discharge of oily wastewater is also increasing. Biochemical treatment, that is, the use of activated sludge for oily wastewater treatment technology is the core of the refinery wastewater treatment process. As a by-product of biochemical treatment, the residual activity of the refinery The output of sludge is also increasing year by year. The composition of residual activated sludge in refineries is relatively complex, and its typical characteristics are as follows: 1. The sludge flocs are mainly composed of microbial cells and their metabolites, and contain rich organic matter; 2. The sludge yield is high and the water content is high. Solid, oil-water emulsion and mixed state of water exist, and it...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C02F11/00C02F11/12C02F11/04C02F11/127
CPCC02F11/00C02F11/12C02F11/04C02F11/127
Inventor 王庆宏陈春茂王鑫詹亚力李晋梁家豪靳峰张仁忠
Owner CHINA UNIV OF PETROLEUM (BEIJING)