CN118142335A - Automatic slurry supplementing flue gas desulfurization system - Google Patents

Automatic slurry supplementing flue gas desulfurization system Download PDF

Info

Publication number
CN118142335A
CN118142335A CN202410491609.7A CN202410491609A CN118142335A CN 118142335 A CN118142335 A CN 118142335A CN 202410491609 A CN202410491609 A CN 202410491609A CN 118142335 A CN118142335 A CN 118142335A
Authority
CN
China
Prior art keywords
lime slurry
flue gas
slurry
lime
pipeline
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
CN202410491609.7A
Other languages
Chinese (zh)
Inventor
邝江华
王秦
王亲雄
曹万宝
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Hunan Chenzhou Mining Industry Co ltd
Original Assignee
Hunan Chenzhou Mining Industry Co ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Hunan Chenzhou Mining Industry Co ltd filed Critical Hunan Chenzhou Mining Industry Co ltd
Priority to CN202410491609.7A priority Critical patent/CN118142335A/en
Publication of CN118142335A publication Critical patent/CN118142335A/en
Pending legal-status Critical Current

Links

Landscapes

  • Treating Waste Gases (AREA)

Abstract

The application discloses a flue gas desulfurization system capable of automatically supplementing slurry, which comprises a desulfurization tower, a lime slurry circulating pool, a slurry mixing barrel and a PLC control cabinet, wherein the bottom of the desulfurization tower is communicated with the lime slurry circulating pool through an overflow chute, a flue gas outlet of the desulfurization tower is provided with a sulfur dioxide concentration detector, the lime slurry circulating pool is connected with a spray pipeline extending into the desulfurization tower, a spray pump is arranged on the spray pipeline, and the lime slurry circulating pool is provided with a pH meter; the slurry mixing barrel is communicated with the lime slurry circulating pool through a lime slurry supplementing pipeline, a lime slurry supplementing valve is arranged on the lime slurry supplementing pipeline, and the sulfur dioxide concentration detector, the pH meter and the lime slurry supplementing valve are all electrically connected with the PLC control cabinet. The flue gas desulfurization system realizes the automatic supplement of lime slurry, thereby taking into account the flue gas desulfurization effect and the full utilization of the lime slurry.

Description

Automatic slurry supplementing flue gas desulfurization system
Technical Field
The invention relates to the technical field of flue gas desulfurization, in particular to a flue gas desulfurization system capable of automatically supplementing slurry.
Background
The flue gas desulfurization system mainly comprises a desulfurization tower and a lime slurry circulating pool, and utilizes lime slurry to realize desulfurization treatment of flue gas by spraying the lime slurry to the flue gas.
At present, whether the lime slurry circulating tank is replenished with fresh lime slurry is generally judged by manpower according to experience, and the defects are that: on one hand, the pH value of lime slurry sprayed to the flue gas is too low due to untimely supplementing of fresh lime slurry, so that desulfurization of the flue gas can not reach the standard; on the other hand, the lime slurry is not fully utilized and discharged, so that the pH value of the discharged lime slurry is too high to influence the treatment cost of the tail sand water.
Disclosure of Invention
Therefore, the invention aims to provide a flue gas desulfurization system capable of automatically supplementing slurry so as to realize automatic supplementation of lime slurry, thereby achieving both flue gas desulfurization effect and full utilization of lime slurry.
The invention solves the problems by the following technical means:
The flue gas desulfurization system capable of automatically supplementing slurry comprises a desulfurization tower, a lime slurry circulating tank, a slurry mixing barrel and a PLC control cabinet, wherein the bottom of the desulfurization tower is communicated with the lime slurry circulating tank through an overflow chute, a sulfur dioxide concentration detector is arranged at a flue gas outlet of the desulfurization tower, the lime slurry circulating tank is connected with a spray pipeline extending into the desulfurization tower, a spray pump is arranged on the spray pipeline, and a pH meter is arranged in the lime slurry circulating tank; the slurry mixing barrel is communicated with the lime slurry circulating pool through a lime slurry supplementing pipeline, a lime slurry supplementing valve is arranged on the lime slurry supplementing pipeline, and the sulfur dioxide concentration detector, the pH meter and the lime slurry supplementing valve are all electrically connected with the PLC control cabinet.
Further, the lime slurry circulating tank is provided with a liquid level meter, and the liquid level meter is electrically connected with the PLC control cabinet.
Further, the lime slurry circulating tank is connected with a slag discharging pipeline.
Further, a slag discharge pump is arranged on the slag discharge pipeline and is electrically connected with the PLC control cabinet.
Further, the lime slurry circulation tank is provided with a stirrer.
Further, the size mixing barrel is also provided with a stirrer.
The invention has the beneficial effects that:
The application discloses a flue gas desulfurization system capable of automatically supplementing slurry, which comprises a desulfurization tower, a lime slurry circulating pool, a slurry mixing barrel and a PLC (programmable logic controller) control cabinet, wherein the bottom of the desulfurization tower is communicated with the lime slurry circulating pool through an overflow chute; the slurry mixing barrel is communicated with the lime slurry circulating pool through a lime slurry supplementing pipeline, a lime slurry supplementing valve is arranged on the lime slurry supplementing pipeline, and the sulfur dioxide concentration detector, the pH meter and the lime slurry supplementing valve are all electrically connected with the PLC control cabinet. The flue gas desulfurization system realizes the automatic supplement of lime slurry, thereby taking into account the flue gas desulfurization effect and the full utilization of the lime slurry.
Drawings
The invention is further described below with reference to the drawings and examples.
FIG. 1 is a schematic diagram of a preferred embodiment of the present invention.
Detailed Description
The invention will be described in detail below with reference to the accompanying drawings, as shown in fig. 1: the flue gas desulfurization system capable of automatically supplementing slurry comprises a desulfurization tower 1, a lime slurry circulating tank 2, a slurry mixing barrel 3 and a PLC control cabinet 10, wherein the bottom of the desulfurization tower is communicated with the lime slurry circulating tank through an overflow chute 12, a flue gas outlet of the desulfurization tower is provided with a sulfur dioxide concentration detector 6, the lime slurry circulating tank is connected with a spray pipeline 13 extending into the desulfurization tower, a spray pump 5 is arranged on the spray pipeline, and the lime slurry circulating tank is provided with a pH meter 8; the slurry mixing barrel is communicated with the lime slurry circulating pool through a lime slurry supplementing pipeline 15, a lime slurry supplementing valve 4 is arranged on the lime slurry supplementing pipeline, and the sulfur dioxide concentration detector, the pH meter and the lime slurry supplementing valve are all electrically connected with the PLC control cabinet.
When the lime slurry desulfurization device works, lime slurry in the lime slurry circulating pool is pumped to the desulfurization tower through the spray pump, then sprayed to flue gas, the flue gas is desulfurized by the lime slurry, and the reacted lime slurry is returned to the lime slurry circulating pool through the overflow chute; when the sulfur dioxide concentration detector detects that the sulfur dioxide concentration exceeds a set value, or the pH meter detects that the pH value is lower than the set value, a signal is fed back to the PLC control cabinet, the opening of the lime slurry supplementing valve is controlled through the PLC control cabinet, and fresh lime slurry is supplemented into the lime slurry circulating pool, so that the pH value of the lime slurry is improved, and the desulfurization capacity of the lime slurry is improved.
As a further improvement to the above technical scheme, the lime slurry circulation tank is provided with a liquid level meter 7, and the liquid level meter is electrically connected with the PLC control cabinet. In the desulfurization reaction process, or in the lime slurry supplementing process, the liquid level meter is used for detecting the liquid level of the lime slurry circulating tank, and feeding back a liquid level signal to the PLC control cabinet, and the PLC control cabinet is used for controlling the opening and closing of the lime slurry supplementing valve, so that the reasonable liquid level of the lime slurry circulating tank is ensured.
As a further improvement to the above technical solution, the lime slurry circulation tank is connected with a slag discharge pipeline 14. The slag discharging pipeline is provided with a slag discharging pump 9, and the slag discharging pump is electrically connected with the PLC control cabinet. The slag discharging function is realized by controlling the start and stop of the slag discharging pump through the PLC control cabinet.
As a further improvement to the above technical solution, both the lime mud circulation tank and the mixing drum are provided with a stirrer 11. Lime slurry is stirred by a stirrer, so that the uniformity of the lime slurry can be improved.
Finally, it is noted that the above embodiments are only for illustrating the technical solution of the present invention and not for limiting the same, and although the present invention has been described in detail with reference to the preferred embodiments, it should be understood by those skilled in the art that modifications and equivalents may be made thereto without departing from the spirit and scope of the technical solution of the present invention, which is intended to be covered by the scope of the claims of the present invention.

Claims (6)

1. The utility model provides an automatic flue gas desulfurization system of moisturizing which characterized in that: the device comprises a desulfurization tower, a lime slurry circulating pool, a slurry mixing barrel and a PLC control cabinet, wherein the bottom of the desulfurization tower is communicated with the lime slurry circulating pool through an overflow chute, a sulfur dioxide concentration detector is arranged at a flue gas outlet of the desulfurization tower, the lime slurry circulating pool is connected with a spray pipeline extending into the desulfurization tower, a spray pump is arranged on the spray pipeline, and a pH meter is arranged in the lime slurry circulating pool; the slurry mixing barrel is communicated with the lime slurry circulating pool through a lime slurry supplementing pipeline, a lime slurry supplementing valve is arranged on the lime slurry supplementing pipeline, and the sulfur dioxide concentration detector, the pH meter and the lime slurry supplementing valve are all electrically connected with the PLC control cabinet.
2. The automatic slurry feed flue gas desulfurization system of claim 1, wherein: the lime slurry circulating tank is provided with a liquid level meter, and the liquid level meter is electrically connected with the PLC control cabinet.
3. The automatic slurry-replenishing flue gas desulfurization system according to claim 2, wherein: the lime slurry circulating tank is connected with a slag discharging pipeline.
4. A flue gas desulfurization system for automatic slurry make-up according to claim 3, wherein: the slag discharging pipeline is provided with a slag discharging pump, and the slag discharging pump is electrically connected with the PLC control cabinet.
5. The automatic slurry-replenishing flue gas desulfurization system according to claim 4, wherein: the lime slurry circulating tank is provided with a stirrer.
6. The automatic slurry-replenishing flue gas desulfurization system according to claim 5, wherein: the size mixing barrel is also provided with a stirrer.
CN202410491609.7A 2024-04-23 2024-04-23 Automatic slurry supplementing flue gas desulfurization system Pending CN118142335A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN202410491609.7A CN118142335A (en) 2024-04-23 2024-04-23 Automatic slurry supplementing flue gas desulfurization system

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN202410491609.7A CN118142335A (en) 2024-04-23 2024-04-23 Automatic slurry supplementing flue gas desulfurization system

Publications (1)

Publication Number Publication Date
CN118142335A true CN118142335A (en) 2024-06-07

Family

ID=91301022

Family Applications (1)

Application Number Title Priority Date Filing Date
CN202410491609.7A Pending CN118142335A (en) 2024-04-23 2024-04-23 Automatic slurry supplementing flue gas desulfurization system

Country Status (1)

Country Link
CN (1) CN118142335A (en)

Similar Documents

Publication Publication Date Title
CN107185385A (en) A kind of spuious flue gas during smelting wet dedusting of atm number, sulfur method
CN107224862A (en) It is a kind of to carry out low concentration SO using fuzzy alkali adding method2The device and method of flue gas desulfurization
CN101844036A (en) Wet flue gas desulfurization (WFGD) process for gypsum through oxidization in tower by using calcium-based strongly basic substance
CN118142335A (en) Automatic slurry supplementing flue gas desulfurization system
CN105709586B (en) A kind of flue gases of cock oven desulphurization system matches liquid, feed liquid method and device
CN108130147A (en) A kind of biogas desulfurization purifier
CN111603903A (en) Double-alkali desulphurization device
CN104759194B (en) The method of flue gas desulfurization
CN201669051U (en) Calcium oxide base strong-alkali absorption device inside wet flue gas desulfurization tower
CN205084614U (en) Marine desulfurization system
CN210131519U (en) Automatic dosing system for carbon black flue gas desulfurization
CN107261799B (en) Device and method for preventing lime milk of smelting desulfurization system from scaling
CN212687907U (en) Lime slurry preparation system for waste incineration
CN205613265U (en) Sodium calcium dual alkali scrubbing FGD process automatic cycle backward flow regeneration system
CN110655254B (en) Coke oven flue gas carbon-based catalytic desulfurization byproduct dilute sulfuric acid recovery treatment method
CN210229611U (en) Flue gas desulfurization system
CN112744946A (en) Lime wet flue gas desulfurization effluent treatment plant
CN202224051U (en) Double-alkali desulfurizer with exterior tower circulation and independent oxidation
CN219964039U (en) Desulfurization wastewater treatment system
CN217367819U (en) Wet flue gas desulfurization filtrate water recycle system
CN205061896U (en) Change grey system
CN218249506U (en) Boiler flue gas wet desulphurization process system
CN109821383A (en) A kind of intelligence prevention and control of air pollution system and method
CN219091641U (en) Device for rapidly controlling SO2 emission concentration
CN204134458U (en) A kind of emergency pool that doublely can do loop slurry system blending tank and recycle slurry flow container

Legal Events

Date Code Title Description
PB01 Publication
SE01 Entry into force of request for substantive examination