CN110947254A - Heating system of bag type dust collector of waste incineration power plant - Google Patents

Heating system of bag type dust collector of waste incineration power plant Download PDF

Info

Publication number
CN110947254A
CN110947254A CN201911361637.2A CN201911361637A CN110947254A CN 110947254 A CN110947254 A CN 110947254A CN 201911361637 A CN201911361637 A CN 201911361637A CN 110947254 A CN110947254 A CN 110947254A
Authority
CN
China
Prior art keywords
air
type dust
dust collector
bag
pipe
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
CN201911361637.2A
Other languages
Chinese (zh)
Inventor
赵娜娜
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.)
Shenzhen Energy Environmental Engineering Co Ltd
Original Assignee
Shenzhen Energy Environmental Engineering 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 Shenzhen Energy Environmental Engineering Co Ltd filed Critical Shenzhen Energy Environmental Engineering Co Ltd
Priority to CN201911361637.2A priority Critical patent/CN110947254A/en
Publication of CN110947254A publication Critical patent/CN110947254A/en
Pending legal-status Critical Current

Links

Images

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D46/00Filters or filtering processes specially modified for separating dispersed particles from gases or vapours
    • B01D46/02Particle separators, e.g. dust precipitators, having hollow filters made of flexible material
    • B01D46/023Pockets filters, i.e. multiple bag filters mounted on a common frame
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D46/00Filters or filtering processes specially modified for separating dispersed particles from gases or vapours
    • B01D46/42Auxiliary equipment or operation thereof
    • B01D46/4263Means for active heating or cooling

Landscapes

  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Chimneys And Flues (AREA)

Abstract

The utility model provides a waste incineration power plant bag collector heating system, includes sack cleaner, induced air system and main heating circulation system, and the induced air system includes air-supply line, draught fan, exhaust pipe, muffler and induced air system in proper order with the air current direction and connects the chimney pipe, and main heating circulation system includes air-supply line interface, air heater aspiration channel, air-supply line valve, air heater exhaust pipe in proper order with the air current direction. And a shared hot smoke system is also arranged and comprises a shared communicating pipe, the inlet of the shared communicating pipe is connected with the exhaust pipe of each induced air system through each eduction pipe, and the outlet of the shared communicating pipe is connected with the suction pipe interface of the hot air self-circulation system of each bag type dust collector through each shunt pipe. When the main heater of the bag-type dust collector frequently breaks down, the hot smoke of other running induced air systems can be used for heating the bag-type dust collector with the fault through the shared hot smoke system, so that the bag-type dust collector with the fault can normally run.

Description

Heating system of bag type dust collector of waste incineration power plant
Technical Field
The invention relates to a flue gas waste heat recycling system, in particular to a heating system of a bag type dust collector of a waste incineration power plant.
Background
A flue gas purification treatment system of a waste incineration plant is provided with a semi-dry reaction tower, an atomizer, a bag-type dust remover, active carbon, lime slurry and other systems. Wherein the sack cleaner is one of the waste incineration power plant flue gas processing system key equipment, and the sack cleaner function has two aspects: firstly, separating dust and solid particles in the flue gas at an inlet, and then discharging dust-free clean gas at an outlet; secondly, the dust adhered to the filter bag contains lime slurry and activated carbon, so that the neutralization reaction can be continued and harmful substances in the dust can be adsorbed.
The preheating circulation of the bag-type dust collector is an important part of the bag-type dust collector, a main heater of the bag-type dust collector preheats a centering box body before cold start in design, so that the temperature in a cabin is preheated to more than 140 ℃ from the ambient temperature within 8 hours, a smoke inlet door and a smoke outlet door are in a closed state before a hot air circulation system of the bag-type dust collector is started, and the box body of the bag-type dust collector is in a closed hot air self-circulation state. The best effect can be achieved only by meeting the condition that the filter bag in the bag-type dust collector removes the dust of the smoke, and meanwhile, the damage to the bag-type dust collector in the injection process after the hot smoke meets with the cold air in the dust collector and is subjected to condensation is prevented. However, in actual operation, the main heater of the bag-type dust collector is found to be frequently broken down, so that the temperature of the chamber cannot meet the requirement.
Disclosure of Invention
In order to overcome the problems in the prior art, the invention provides a heating system of bag-type dust collectors of a waste incineration power plant, which is characterized in that a shared hot smoke system is arranged and comprises a shared communicating pipe, the inlet of the shared communicating pipe is connected with the exhaust pipes of all air induction systems through all eduction pipes, and the outlet of the shared communicating pipe is connected with the suction pipe interfaces of the hot air self-circulation systems of all bag-type dust collectors through all shunt pipes. When the main heater of the bag-type dust collector frequently breaks down, so that the temperature of the bin cannot meet the requirement, the bag-type dust collector with the fault can be heated by sharing the hot smoke system and utilizing the hot smoke of other running induced air systems, and the bag-type dust collector with the fault can be ensured to normally run.
The technical scheme includes that the bag type dust collector heating system of the waste incineration power plant comprises a bag type dust collector, an air inducing system and a main heating circulating system, wherein the air inducing system sequentially comprises an air inlet pipe, an induced draft fan, an exhaust pipe, a silencer and an air inducing system in an air flow direction, the air inlet pipe is connected with the bag type dust collector, and the air inducing system is connected with a chimney pipe to discharge smoke to a chimney; the main heating circulation system comprises an air suction pipe interface, an air heater air suction pipe, an air suction pipe valve, an air heater and an air heater exhaust pipe in sequence along the air flow direction, wherein the air heating system air suction pipe is connected with an interface of the bag type dust collector and sucks air from the interface, the air heater exhaust pipe is connected with another interface of the bag type dust collector and provides hot air to the air heater, and the air heater continuously provides hot air to the bag type dust collector in a circulating manner.
The invention has the beneficial effects that: the utility model provides a msw incineration power plant bag collector heating system, is through setting up the hot cigarette system of sharing, and the hot cigarette system of sharing is including sharing communicating pipe, the entry of sharing communicating pipe is connected with the exhaust pipe of each induced air system through each stand-off pipe, the export of sharing communicating pipe is through the inlet scoop interface connection of each shunt tubes and each bag collector's hot-blast self-circulation system. When the main heater of the bag-type dust collector frequently breaks down, so that the temperature of the bin cannot meet the requirement, the bag-type dust collector with the fault can be heated by sharing the hot smoke system and utilizing the hot smoke of other running induced air systems, and the bag-type dust collector with the fault can be ensured to normally run.
Drawings
Fig. 1-3 are schematic diagrams of system arrangements according to one embodiment of the prior art. Fig. 1 is a front view, fig. 2 is a plan view, and fig. 3 is an enlarged view of a part of the structure.
Fig. 4 and 6 are schematic diagrams of the system layout of the first embodiment of the present invention. Fig. 4 is a front view, fig. 5 is a plan view, and fig. 6 is a partially enlarged schematic view of the structure.
In the figure:
bag-type dust collectors 1A and 1, bag-type dust collectors 1B and 2,
2A, 1 # induced draft system; 2B, 2 # induced draft system;
2A1, No. 1 induced draft fan; 2B1 and No. 2 induced draft fan;
2A21, No. 1 air inlet pipe, 3A22 and No. 1 exhaust pipe; 2B21, No. 2 air inlet pipe, 3B22 and No. 2 exhaust pipe;
2a3, No. 1 muffler; 2B3, No. 2 muffler;
the 2A4 No. 1 induced draft system is connected with a chimney; 2B4, 2 # induced draft system connects chimney;
3A, No. 1 main heating circulation system; no. 3B and No. 2 main heating circulation systems,
3a1, No. 1 air heater; 3B1, No. 2 air heater;
3A21, No. 1 air suction pipe of air heater, 3A22, No. 1 air exhaust pipe of air heater; no. 3B21 air suction pipe of air heater No. 2, No. 3B22 air exhaust pipe of air heater No. 2;
3a3, No. 1 draft tube valve; 3B3, No. 2 draft tube valve;
3A4, No. 1 suction tube interface; 3B4, No. 2 suction tube interface;
4. a shared hot smoke system; 4.1 sharing the communicating pipe;
4A1, No. 1 eduction tube; 4B1, No. 2 eduction tube;
4A2, No. 1 outlet pipe valve; 4B2, No. 2 outlet pipe valve;
4a3, shunt No. 1; 4B3, No. 2 shunt tube.
Detailed Description
Fig. 1-3 are schematic diagrams of system arrangements according to one embodiment of the prior art. Fig. 1 is a front view, fig. 2 is a plan view, and fig. 3 is an enlarged view of a part of the structure. In the prior art, the heating system of the bag-type dust collector of the waste incineration power plant comprises a bag-type dust collector 1A and a bag-type dust collector 2B of a waste incineration power plant, an air induction system 2A and 2B of the waste incineration power plant, a main heating circulation system 3A of the waste incineration power plant and a main heating circulation system 3B of the waste incineration power plant.
The drawing shows that No. 1 induced air system 2A includes No. 1 air-supply line 2A21, No. 1 draught fan 2A1, No. 1 exhaust pipe 2A22, No. 1 muffler 2A3 and No. 1 induced air system in proper order with the air current direction and connects chimney 2A4, air-supply line 2A21 is connected with bag dust remover, induced air system connects chimney 2A4 and arranges the flue gas to the chimney. No. 1 main heating cycle system 3A includes No. 1 aspiration channel interface 3A4, No. 1 air heater aspiration channel 3A21, No. 1 aspiration channel valve 3A3, No. 1 air heater 3A1, No. 1 air heater exhaust pipe 3A22 in proper order with the air current direction, No. 1 air heating system aspiration channel 3A21 with an interface connection of No. 1 bag collector inhales from it, No. 1 air heater exhaust pipe 3A22 with another interface connection of No. 1 bag collector provides hot-blast to it, warp No. 1 air heater 3A1 constantly to No. 1 bag collector circulation provides hot-blast.
The drawing shows that No. 2 induced draft system 2B includes No. 2 air-supply line 2B21, No. 2 draught fan 2B1, No. 2 exhaust pipe 2B22, No. 2 muffler 2B3 and No. 2 induced draft system in proper order with the air current direction and connects chimney 2B4, air-supply line 2B21 is connected with bag dust remover, induced draft system connects chimney 2B4 and arranges the flue gas to the chimney. No. 2 main heating cycle system 3B includes No. 2 aspiration channel interface 3B4, No. 2 air heater aspiration channel 3B21, No. 2 aspiration channel valves 3B3, No. 2 air heater 3B1, No. 2 air heater exhaust pipe 3B22 in proper order with the air current direction, No. 2 air heating system aspiration channel 3B21 with an interface connection of No. 2 bag collector inhales from it, No. 2 air heater exhaust pipe 3B22 with No. 2 another interface connection of bag collector provides the hot-blast to it, warp No. 2 air heater 3B1 constantly to No. 2 bag collector circulation provides the hot-blast.
The primary heater systems of the individual baghouses of the waste incineration system are shown to be operated independently.
In the actual operation process, before the hot air circulating system of the bag type dust collector is started, the smoke inlet door and the smoke outlet door are in a closed state, and the box body of the bag type dust collector is in a closed hot air self-circulating state. The best effect can be achieved only by meeting the condition that the filter bag in the bag-type dust collector removes dust from smoke, and meanwhile, the bag-type dust collector is prevented from being damaged in the injection process after hot smoke meets with cold air in the dust collector and is subjected to condensation. However, in actual operation, the main heater of the bag-type dust collector is found to be frequently in fault, so that the temperature of the bin cannot meet the requirement. The present invention suggests that in this example, only two bag house collectors and their related systems are shown, whereas in actual operation, the number of bag house collectors and their related systems of the waste incineration system exceeds two.
Fig. 4-6 are schematic system layouts according to a first embodiment of the present invention. Fig. 4 is a front view, fig. 5 is a plan view, and fig. 6 is a partially enlarged schematic view of the structure. The figure shows that, different from the prior art, in this example, a bag collector heating system of a waste incineration power plant is further provided with a shared hot smoke system 4, the shared hot smoke system 4 includes a shared communicating pipe 4.1, an inlet of the shared communicating pipe 4.1 is connected with an exhaust pipe 2A22 of a No. 1 induced draft system 2A and an exhaust pipe 2B22 of a No. 2 induced draft system 2B through a No. 1 eduction pipe 4a1 and a No. 2 eduction pipe 4B1, respectively, and an outlet of the shared communicating pipe 4.1 is connected with a No. 1 suction pipe interface 3a4 and a No. 2 suction pipe interface 3B4 through a No. 1 shunt pipe 4A3 and a No. 4B3, respectively.
In the present embodiment, when the main heater of a certain bag-type dust collector frequently fails and the temperature of the bin cannot meet the requirement, the hot smoke of other air inducing systems in operation can be used to heat the bag-type dust collector with the failure through the shared hot smoke system, so as to ensure that the bag-type dust collector with the failure can normally operate.

Claims (1)

1. A bag type dust collector heating system of a waste incineration power plant comprises a bag type dust collector, an air inducing system and a main heating circulating system, wherein the air inducing system sequentially comprises an air inlet pipe, an induced draft fan, an exhaust pipe, a silencer and an air inducing system in the airflow direction and is connected with a chimney pipe; the main heating circulation system comprises an air suction pipe interface, an air heater air suction pipe, an air suction pipe valve, an air heater and an air heater exhaust pipe in sequence along the air flow direction, wherein the air heating system air suction pipe is connected with an interface of the bag type dust collector and sucks air from the interface, the air heater exhaust pipe is connected with another interface of the bag type dust collector and provides hot air to the air heater, and the air heater continuously provides hot air to the bag type dust collector in a circulating manner.
CN201911361637.2A 2019-12-25 2019-12-25 Heating system of bag type dust collector of waste incineration power plant Pending CN110947254A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201911361637.2A CN110947254A (en) 2019-12-25 2019-12-25 Heating system of bag type dust collector of waste incineration power plant

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201911361637.2A CN110947254A (en) 2019-12-25 2019-12-25 Heating system of bag type dust collector of waste incineration power plant

Publications (1)

Publication Number Publication Date
CN110947254A true CN110947254A (en) 2020-04-03

Family

ID=69984150

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201911361637.2A Pending CN110947254A (en) 2019-12-25 2019-12-25 Heating system of bag type dust collector of waste incineration power plant

Country Status (1)

Country Link
CN (1) CN110947254A (en)

Similar Documents

Publication Publication Date Title
CN207963507U (en) A kind of coal base shaft furnace flue gas waste heat recovery system
CN101403506A (en) Calcium carbide stove exhaust combustion and utilization method and device
CN102183155A (en) Smoke high-temperature dust removal and steam and coal gas recovery system and method for calcium carbide furnace
CN203190418U (en) Novel garbage pyrolysis incineration equipment
CN204787776U (en) Enamel fritting furnace
CN211771479U (en) Chain grate-rotary kiln-circular cooler with reheating SCR (Selective catalytic reduction) ultralow emission
CN201285050Y (en) Tail gas combustion utilization apparatus for calcium carbide furnace
CN201724384U (en) Energy-saving environment-friendly high temperature jet type hot blast stove
CN203298336U (en) Air heating furnace smoke energy recycling system
CN211864210U (en) Heating system of bag type dust collector of waste incineration power plant
CN103062893B (en) Pulverized-coal combustion hot water boiler
CN209840118U (en) Energy-conserving RTO heat accumulation formula burns burning furnace
CN110947254A (en) Heating system of bag type dust collector of waste incineration power plant
CN207822773U (en) Exhaust treatment system
CN105486096A (en) Waste-heat utilization method and device for indirect heating type sintering system
CN104197733B (en) Regenerative cycles device in Gas heating furnace high-temperature burns carbon distribution device and technique
CN204534546U (en) Biomass boiler environmental protection and energy saving control system
WO2021128108A1 (en) Bag filter heating system for waste incineration power plant
CN209893411U (en) Special incinerator pollution-free cleaning system for asphalt smoke
CN209944365U (en) Direct combustion type deodorizing device
CN203286573U (en) Salty waste water burning system
CN207006884U (en) Limekiln high-temp waste gas cyclic utilization system
CN111520731A (en) Direct-combustion backflow heat recovery high-efficiency organic waste gas treatment system and method
CN206222953U (en) Metal smelting-furnace
CN205505032U (en) Heat accumulating type catalytic oxidation device

Legal Events

Date Code Title Description
PB01 Publication
PB01 Publication
SE01 Entry into force of request for substantive examination
SE01 Entry into force of request for substantive examination
CB02 Change of applicant information
CB02 Change of applicant information

Address after: 518046 13th Floor, Times Financial Center, 4001 Shennan Avenue, Futian District, Shenzhen City, Guangdong Province

Applicant after: Shenzhen Energy and environmental protection Co.,Ltd.

Address before: 518046 13th Floor, Times Financial Center, 4001 Shennan Avenue, Futian District, Shenzhen City, Guangdong Province

Applicant before: SHENZHEN ENERGY ENVIRONMENTAL ENGINEERING Co.,Ltd.