Eureka AIR delivers breakthrough ideas for toughest innovation challenges, trusted by R&D personnel around the world.

Biological treatment method, biological treatment system and bioreactor of coal chemical wastewater

A technology for coal chemical wastewater and biological treatment, which is applied in the field of coal chemical wastewater treatment and wastewater treatment containing high concentrations of organic pollutants and ammonia nitrogen. question

Active Publication Date: 2013-01-16
BEIJING CYCLE COLUMBUS ENVIRONMENTAL SCI & TECH
View PDF3 Cites 13 Cited by
  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

During the biological aerobic degradation process of the traditional activated sludge method, the degradation rate of such substances is very slow or cannot be degraded; on the other hand, the aerobic degradation process may produce long-chain acids and ketones with the ring opening of the PAH , lipids and other substances that are more difficult to be biodegraded, resulting in generally higher COD of treated wastewater, at 300-500mg / L
[0006] (2) On the other hand, the traditional biological process often uses a single aerobic reaction tank to remove organic matter and ammonia nitrogen, that is, aerobic heterotrophic bacteria and nitrifying bacteria grow simultaneously, and the biological process uses a high sludge return ratio (>150%) , so that the activated sludge periodically changes the growth conditions and exerts different biological functions, which is not conducive to the formation of functional flora and inhibits the activity of nitrifying bacteria, resulting in low removal efficiency of organic matter in the treatment process, poor operation stability, and high treatment costs
High concentrations of organic matter will inhibit the activity of nitrifying bacteria. Nitrifying reactions only occur at the end of the aerobic reaction tank, and nitrifying bacteria grow slowly, have a long generation cycle, and have poor toxicity resistance, which affects the stability of the biological process and increases the treatment cost.
[0007] (3) Coal chemical industry wastewater contains a high concentration of ammonia nitrogen. The traditional biological denitrification process takes a long time and consumes a lot of power and chemicals, resulting in high wastewater treatment costs.
However, it adopts one-step nitrification, short-range nitrification reaction and full-process nitrification reaction at the same time, and in order to reduce the nitrite content in the effluent water and reduce the toxicity of the effluent, it is necessary to focus on the full-process nitrification. Therefore, the oxygen demand and alkali consumption are relatively high. High processing cost and low processing rate

Method used

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
View more

Image

Smart Image Click on the blue labels to locate them in the text.
Viewing Examples
Smart Image
  • Biological treatment method, biological treatment system and bioreactor of coal chemical wastewater
  • Biological treatment method, biological treatment system and bioreactor of coal chemical wastewater
  • Biological treatment method, biological treatment system and bioreactor of coal chemical wastewater

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0083] The pretreated coal chemical wastewater enters the bottom of the anaerobic reactor, and the effluent elevations of the reactors at all levels decrease successively. The anaerobic acidification treatment is carried out in the anaerobic reactor, and the hydraulic retention time of the anaerobic reactor is 7 hours. The effluent from the anaerobic reactor enters the water distribution system at the bottom of the anoxic reactor, and at the same time, the returning nitrification liquid (from the secondary and tertiary aerobic reactors, with a reflux ratio of 6:1) also flows back to the water distribution system, and the dissolved oxygen in the anoxic reactor The concentration is 0.5mg / L, the N / C value is 3, the temperature is 25°C, the pH is 9, and the hydraulic retention time is about 15 hours. The effluent from the anoxic reactor flows into the first-stage aerobic reactor by itself, and at the same time, a certain amount of Na 2 CO 3 and Na 2 HPO 3 . The dissolved oxyg...

Embodiment 2

[0085] The pretreated coal chemical wastewater enters the bottom of the anaerobic reactor, and the effluent elevations of the reactors at all levels decrease successively. The anaerobic acidification treatment is carried out in the anaerobic reactor, and the hydraulic retention time of the anaerobic reactor is 5 hours. The effluent from the anaerobic reactor enters the water distribution system at the bottom of the anoxic reactor, and at the same time, the returning nitrification liquid (from the secondary and tertiary aerobic reactors, with a reflux ratio of 2:1) also flows back to the water distribution system, and the dissolved oxygen in the anoxic reactor The concentration is 0.8mg / L, the N / C value is 2.5, the temperature is 38°C, the pH is 7.7, and the hydraulic retention time is about 40 hours. The effluent from the anoxic reactor flows into the first-stage aerobic reactor by itself, and at the same time, a certain amount of Na 2 CO 3 and Na 2 HPO 3 . The dissolved ...

Embodiment 3

[0087] The pretreated coal chemical wastewater enters the bottom of the anaerobic reactor, and the effluent elevations of the reactors at all levels decrease successively. The anaerobic acidification treatment is carried out in the anaerobic reactor, and the hydraulic retention time of the anaerobic reactor is 15 hours. The effluent from the anaerobic reactor enters the water distribution system at the bottom of the anoxic reactor, and at the same time, the returning nitrification liquid (from the secondary and tertiary aerobic reactors, with a reflux ratio of 8:1) also flows back to the water distribution system, and the dissolved oxygen in the anoxic reactor The concentration is 0.6mg / L, the N / C value is 3.5, the temperature is 20°C, the pH is 9.3, and the hydraulic retention time is about 10 hours. The effluent from the anoxic reactor flows into the first-stage aerobic reactor by itself, and at the same time, a certain amount of Na 2 CO 3 and Na 2 HPO 3. The dissolved ...

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
Login to View More

PUM

No PUM Login to View More

Abstract

The invention relates to a biological treatment method of coal chemical wastewater, which adopts a biological reaction-muddy water separation integrated bioreactor. The method comprises the following steps of: sequentially feeding materialized and pre-treated coal chemical wastewater into an anaerobic bioreactor, an anoxic bioreactor, a first-stage aerobiotic bioreactor, a second-stage aerobiotic bioreactor and a third-stage aerobiotic bioreactor, selecting each aerobiotic bioreactor to discharge water and inflow into the anoxic bioreactor; and carrying out anaerobic acidification treatment by the anaerobic reactor, reinforcing a biological denitrification reaction in the anoxic reactor to remove non-gradable organic matters, completely decarbonizing by the first-stage aerobiotic bioreactor, and realizing the short-course nitratlon reaction and the whole-course nitratlon reaction by the second-stage aerobiotic bioreactor and the third-stage aerobiotic bioreactor, wherein the sludge concentration in the reactor can be guaranteed to be greater than 8mg / L due to the biological reaction-muddy water separation integrated bioreactor, the sludge age is greater than 60 days, the specific strains can be preferably cultured, and the function realization of a novel method can be guaranteed. The coal chemical wastewater is treated by the method, so that the discharged water can reach the requirement of the national wastewater comprehensive discharge standard.

Description

technical field [0001] The invention relates to the field of wastewater treatment, in particular to the field of coal chemical industry wastewater treatment containing high-concentration organic pollutants and ammonia nitrogen. Background technique [0002] Coal chemical industry wastewater is the wastewater generated during the coal chemical production process during high-temperature coal coking, gas purification, coking product recovery and refining. There are many kinds of pollutants in coal chemical industry wastewater with complex components, such as organic pollutants such as phenols, benzene series, nitrogen-containing heterocyclic aromatic hydrocarbons, polycyclic aromatic hydrocarbons, toxic inorganic pollutants such as sulfides, rhodanides, cyanides, and high concentration of ammonia nitrogen. Biological method is a treatment technology widely used at present, among which the traditional biological denitrification process (A / O process) and its improved process (su...

Claims

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
Login to View More

Application Information

Patent Timeline
no application Login to View More
IPC IPC(8): C02F3/30
Inventor 李海波李玉平盛宇星林琳刘永胜贺荣华
Owner BEIJING CYCLE COLUMBUS ENVIRONMENTAL SCI & TECH
Who we serve
  • R&D Engineer
  • R&D Manager
  • IP Professional
Why Eureka
  • Industry Leading Data Capabilities
  • Powerful AI technology
  • Patent DNA Extraction
Social media
Eureka Blog
Learn More
PatSnap group products