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Aeration control system and aeration control method

A control system and aeration technology, applied in water aeration, chemical instruments and methods, water/sludge/sewage treatment, etc., can solve problems that are expensive, take hours or even days, and have not yet been fully popularized

Active Publication Date: 2019-06-28
尚川(北京)水务有限公司 +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

The basic principle of aeration control using water quality indicators as feed-forward is to calculate the amount of oxygen that needs to be provided through the concentration of pollutants. However, most of the sewage water quality indicators rely on experimental measurements, and the measurement time takes hours or even days. This has an impact on real-time control. not big
Online water quality testing instruments also have a delay of several hours, are expensive, and have not yet been fully popularized

Method used

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  • Aeration control system and aeration control method

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0081] Set the desired dissolved oxygen concentration. The set dissolved oxygen value is to make the actual aeration amount as close or consistent as possible to the expected value by changing the aeration amount;

[0082] Select the control mode according to the difference between the DO actual value and the set value (expected value);

[0083] According to the difference between the DO set value and the DO actual value, the measured value of the oxygen consumption rate (OUR) tester, the measured value of the oxygen transfer efficiency (OTE) tester and the above Calculate the required aeration volume according to the actual air volume;

[0084] Adjust the fan according to the aeration rate; and when there is a large impact load or other factors that cause the deviation between the actual value of DO and the set value to exceed ±k1, the system will automatically switch to the DO feedback control mode, so that the actual value of DO can be adjusted rapidly. Back to the normal ...

Embodiment 2

[0090] The volume of the aeration tank is 0.25m 3 , Since the measurement period of the OUR measuring instrument is 15 minutes, the control period is set to 15min, SOTE=20%, SOTR=0.03kg / h, k=0.75, C * ∞20 is the saturated dissolved oxygen value at 20°C;

[0091] The initial setting value of dissolved oxygen is 2. After connecting the OUR meter, OTE meter, DO meter and aeration system to the PLC, the aeration control can be started. The three values ​​of OUR, OTE and DO are The change will be transmitted to the PLC control cabinet through the signal transmission line, and the actual required air volume will be calculated, and the command will be transmitted to the flow control valve to achieve the command value by changing its opening, and the actual air volume value will be displayed on the signal screen through the signal line.

[0092] Under stable conditions, the OUR and OTE values ​​do not change much, and the control quality of dissolved oxygen is stable within the rang...

specific Embodiment

[0094] 1. When OUR=30mg / L·h, DO 设定值 =2.0mg / L, OTE=8%, if the actual dissolved oxygen DO 实际值 =1.5mg / L, then Q=9.21L / min;

[0095] 2. When OUR=30mg / L·h, DO 实际值 When it rises to 2.0mg / L, Q=7.86L / min at this time;

[0096] 3. If OUR=30mg / L·h, k1=0.5mg / L, DO 实际值 When it drops to 1.4mg / L, the system starts DO feedback control, setting β=5, the last aeration Q is 8.48L / min, and now the aeration Q rises to 11.48L / min.

[0097] From 1 to 2, since the actual dissolved oxygen rises from 1.5mg / L to 2mg / L under the action of a large air volume at this time, the aeration volume also decreases accordingly, so that the actual dissolved oxygen gradually falls back closer to the set value ;From 1 to 3, due to |C 设定值 -C 实际值 |>k1(k1=0.5mg / L), start the DO feedback protection system, and the aeration volume is based on |C 设定值 -C 实际值 |The difference is adjusted so that the actual dissolved oxygen value can quickly return to the normal fluctuation range.

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Abstract

The invention discloses an aeration control system. The system comprises a data collecting unit, a PLC control unit and an aeration unit. The data collecting unit comprises an OUR tester, an OTE tester and a DO tester. The PLC control unit comprises hardware such as a control cabinet and a display screen, and control software. The control software particularly is a program for achieving automatic control. The aeration unit comprises an air blower, a micro-hole aeration head and a flow meter. The invention further provides a method for carrying out aeration control through the aeration control system. According to the aeration control system and method, a control mode based on the oxygen uptake rate (OUR) value and the oxygen transfer efficiency (OTE) value and a DO feedback control mode are integrated, the dynamic supply-demand balance of oxygen is finally achieved, the poor water quality problem caused by oxygen supply shortage can be solved, energy waste caused by excessive aeration can also be reduced, and meanwhile the function of evaluating the performance of an aeration system is achieved.

Description

technical field [0001] The invention relates to the field of sewage treatment, in particular to an aeration control system and an aeration control method. Background technique [0002] According to statistics, my country spends nearly 30 billion yuan on sewage treatment and operation every year, and a large part of this is generated by electricity consumption in the sewage treatment process. Usually, the electricity consumption of the aeration system accounts for about 10% of the total electricity consumption of the sewage plant operation. 50% to 70% of the energy consumption, and the aeration link is an indispensable part, so reducing the energy consumption in the aeration stage is the most important thing for the sewage treatment plant to save energy and reduce consumption. The aeration control strategy is to automatically and accurately regulate the aeration volume in the sewage treatment process by using automatic control instruments and related control logic, so as to ac...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C02F7/00
CPCY02W10/10
Inventor 罗涛
Owner 尚川(北京)水务有限公司