CN210434244U - Oxygen-enriched equipment special for water-coal-slurry furnace - Google Patents

Oxygen-enriched equipment special for water-coal-slurry furnace Download PDF

Info

Publication number
CN210434244U
CN210434244U CN201921049307.5U CN201921049307U CN210434244U CN 210434244 U CN210434244 U CN 210434244U CN 201921049307 U CN201921049307 U CN 201921049307U CN 210434244 U CN210434244 U CN 210434244U
Authority
CN
China
Prior art keywords
stop valve
adsorption tower
pneumatic stop
tower
voltage
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.)
Active
Application number
CN201921049307.5U
Other languages
Chinese (zh)
Inventor
董平华
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.)
Hangzhou Fuyang Hunter Gas Equipment Co Ltd
Original Assignee
Hangzhou Fuyang Hunter Gas Equipment 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 Hangzhou Fuyang Hunter Gas Equipment Co Ltd filed Critical Hangzhou Fuyang Hunter Gas Equipment Co Ltd
Priority to CN201921049307.5U priority Critical patent/CN210434244U/en
Application granted granted Critical
Publication of CN210434244U publication Critical patent/CN210434244U/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Images

Landscapes

  • Air Supply (AREA)

Abstract

The utility model provides a special oxygen boosting equipment of coal slurry stove, includes adsorption tower A, adsorption tower B, and the bottom is connected with the air inlet pipeline that is equipped with pneumatic stop valve V1 and pneumatic stop valve V2 between adsorption tower A and the adsorption tower B, its main technical characteristics are in the middle part of adsorption tower A and adsorption tower B intercommunication each other has the voltage-sharing air vent line that is equipped with pneumatic stop valve V7 and pneumatic stop valve V8, connects the voltage-sharing return circuit of ventilating in the middle of the two valves of voltage-sharing air vent line, and the other end of voltage-sharing return circuit of ventilating is in the middle of the two valves of air inlet pipeline. The utility model discloses add voltage-sharing vent line at adsorption tower A, adsorption tower B's middle part, through the switch of adjusting valve, utilize two tower production processes short-lived pressure differentials, make the effective gas of A tower get into the B tower through the voltage-sharing that varies, the A tower is prepared the in-process unfinished effective gas and is regenerated at the B tower, and on the contrary, the reason is the same to reduce voltage, the energy saving.

Description

Oxygen-enriched equipment special for water-coal-slurry furnace
Technical Field
The utility model relates to a special oxygen boosting air separation plant of coal slurry stove.
Background
The water-coal-slurry boiler refers to a boiler using water-coal-slurry as fuel. The coal water slurry is a liquid prepared by mixing about 70% of coal powder, about 30% of water and a small amount of medicament, can be pumped, atomized, stored and transported like oil, and can be directly used for burning of various boilers and kilns. The traditional combustion mode of coal is changed, and the great environment-friendly and energy-saving advantages are displayed. Especially in recent years, after a technical route of waste recycling is adopted, the environment-friendly coal water slurry which is successfully developed can greatly improve the environment-friendly benefit of the coal water slurry on the premise of not increasing the cost. Under the guarantee of rich coal data in China, the coal water slurry also becomes one of the most basic and most economic clean energy sources for replacing oil, gas and other energy sources.
The suspension atomization coal water slurry boiler mainly adopts an atomization combustion mode, generates less evaporation (generally less than 10 t/h), and is more suitable for printing and dyeing enterprises. The suspension atomized water-coal slurry boiler integrates the advantages of fuel oil and coal, and is conveyed in liquid state and atomized and combusted. The combustion efficiency can reach 98-99%, and the thermal efficiency can reach more than 82%. Has the obvious characteristics of low operation cost, energy conservation and environmental protection.
Under the condition, the coal water slurry airflow is radiated by the walls of the hearth and high-temperature flame to quickly heat coal particles suspended in the airflow until enough heat is obtained and a certain temperature is reached, and then the ignition combustion is started. The operation load of the boiler depends on the property of fuel and the operation condition, namely when the boiler load is low, the average smoke temperature of a hearth is reduced, and the smoke temperature of a combustor area is reduced along with the reduction of the average smoke temperature. The lowest operation load of the atomized combustion type water-coal slurry boiler is about 50 percent.
After the oxygen-enriched air separation equipment is combined with the air compressor, the combustion intensity and the combustion efficiency can be improved, and the combustion speed is accelerated. However, when the adsorption tower begins to generate gas, unqualified gas is generated and generally discharged as waste gas, which is not fully utilized, and energy is wasted.
Disclosure of Invention
The utility model provides a special oxygen enrichment equipment of coal water slurry furnace which makes full use of effective gas and saves energy.
The utility model discloses a realize through following technical scheme: the utility model provides a special oxygen boosting equipment of coal slurry stove, including adsorption tower A, adsorption tower B, the bottom is connected with the air inlet pipeline that is equipped with pneumatic stop valve V1 and pneumatic stop valve V2 between adsorption tower A and the adsorption tower B, still parallel connection has the blast pipe that is equipped with pneumatic stop valve V3 and pneumatic stop valve V4, the gas outlet pipeline of top connection pneumatic stop valve V5 and pneumatic stop valve V6 between adsorption tower A and the adsorption tower B, its main technical characteristics be in the middle part of adsorption tower A and adsorption tower B communicates each other has the voltage-sharing vent line that is equipped with pneumatic stop valve V7 and pneumatic stop valve V8, connect the voltage-sharing return airway in the middle of the two valves of voltage-sharing vent line, the other end of voltage-sharing return airway connects in the middle of the two valves of air.
The pressure equalizing and ventilating loop is connected with an air inlet pipe, and a pneumatic stop valve V10 is arranged on the air inlet pipe.
And an air outlet main pipe is connected between the pneumatic stop valve V5 and the pneumatic stop valve V6 of the air outlet pipeline, and the air outlet main pipe is provided with a pneumatic stop valve V9.
The utility model discloses add voltage-sharing vent line at adsorption tower A, adsorption tower B's middle part, through the switch of adjusting valve, utilize two tower production processes short-lived pressure differentials, make the effective gas of A tower get into the B tower through the voltage-sharing that varies, the A tower is prepared the in-process unfinished effective gas and is regenerated at the B tower, and on the contrary, the reason is the same to reduce voltage, the energy saving.
Description of the drawings:
fig. 1 is a front view of the present invention;
fig. 2 is a rear view of the present invention;
fig. 3 is a pipeline connection diagram of the present invention.
The specific implementation mode is as follows:
as shown in fig. 1, fig. 2 and fig. 3, the oxygen enrichment equipment special for the coal water slurry furnace comprises an adsorption tower A and an adsorption tower B, wherein an air inlet pipeline provided with a pneumatic stop valve V1 and a pneumatic stop valve V2 is connected to the bottom between the adsorption tower A and the adsorption tower B, an exhaust pipe provided with a pneumatic stop valve V3 and a pneumatic stop valve V4 is further connected in parallel, an air outlet pipeline provided with a pneumatic stop valve V5 and a pneumatic stop valve V6 is connected to the top between the adsorption tower A and the adsorption tower B, and the oxygen enrichment equipment is characterized in that the middle parts of the adsorption tower A and the adsorption tower B are mutually communicated with a pressure equalizing vent pipeline provided with a pneumatic stop valve V7 and a pneumatic stop valve V8, a pressure equalizing vent loop is connected between two valves of the pressure equalizing vent pipeline, and the other. The pressure equalizing and ventilating loop is connected with an air inlet pipe, and a pneumatic stop valve V10 is arranged on the air inlet pipe. The pneumatic stop valve V5 and the pneumatic stop valve V6 of the gas outlet pipeline are connected with a gas outlet main pipe, and the gas outlet main pipe is provided with a pneumatic stop valve V9.
The working process is as follows: when the gas is fed, the pneumatic stop valve V10 is opened firstly, the gas enters a pressure equalizing and ventilating loop, then the gas enters the adsorption tower A through the pneumatic stop valve V1, oxygen is produced, and gas is discharged from the pneumatic stop valve V5 and the pneumatic stop valve V9;
then, the pneumatic stop valve V10 is closed, the pneumatic stop valve V7 is opened, the pneumatic stop valve V2 is opened, and the gas in the adsorption tower A flows out of a pressure equalizing vent pipeline of the pneumatic stop valve V7 and enters the pneumatic stop valve V2 to the adsorption tower B;
after 7 seconds, the pneumatic stop valve V10 is opened at the same time, air enters, and oxygen exits through the pneumatic stop valve V6 and the pneumatic stop valve V9.
In the second round, the pressure difference between the two towers within a few seconds is utilized in the opposite direction, the unqualified gas enters the tower which does not work through the pressure-equalizing vent pipeline, the oxygen is generated by the re-work, the energy is fully utilized, the discharge of the unqualified gas is reduced, and the energy is saved.

Claims (3)

1. The utility model provides a special oxygen boosting equipment of coal slurry stove, including adsorption tower A, adsorption tower B, the bottom is connected with the air inlet pipeline that is equipped with pneumatic stop valve V1 and pneumatic stop valve V2 between adsorption tower A and the adsorption tower B, still parallel connection has the blast pipe that is equipped with pneumatic stop valve V3 and pneumatic stop valve V4, the gas outlet pipeline of pneumatic stop valve V5 and pneumatic stop valve V6 is connected at the top between adsorption tower A and the adsorption tower B, its characterized in that the middle part of adsorption tower A and adsorption tower B communicates each other has the pressure-equalizing vent line that is equipped with pneumatic stop valve V7 and pneumatic stop valve V8, the middle pressure-equalizing vent line that connects of two valves of pressure-equalizing vent line, the other end in pressure-equalizing vent line connects in the middle of two valves of air.
2. The special oxygen enrichment equipment for the coal-water slurry furnace as claimed in claim 1, wherein the pressure equalizing and ventilating loop is connected with an air inlet pipe, and a pneumatic stop valve V10 is arranged on the air inlet pipe.
3. The special oxygen enrichment equipment for the coal-water slurry furnace as claimed in claim 1, wherein the pneumatic stop valve V5 and the pneumatic stop valve V6 of the gas outlet pipeline are connected with a gas outlet main pipe, and the gas outlet main pipe is provided with a pneumatic stop valve V9.
CN201921049307.5U 2019-07-08 2019-07-08 Oxygen-enriched equipment special for water-coal-slurry furnace Active CN210434244U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201921049307.5U CN210434244U (en) 2019-07-08 2019-07-08 Oxygen-enriched equipment special for water-coal-slurry furnace

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201921049307.5U CN210434244U (en) 2019-07-08 2019-07-08 Oxygen-enriched equipment special for water-coal-slurry furnace

Publications (1)

Publication Number Publication Date
CN210434244U true CN210434244U (en) 2020-05-01

Family

ID=70404943

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201921049307.5U Active CN210434244U (en) 2019-07-08 2019-07-08 Oxygen-enriched equipment special for water-coal-slurry furnace

Country Status (1)

Country Link
CN (1) CN210434244U (en)

Similar Documents

Publication Publication Date Title
CN101556039A (en) Oxygen-enriched burner
CN209027308U (en) A kind of low-temperature flue gas waste heat recycling dragging system of efficient stable
CN210434244U (en) Oxygen-enriched equipment special for water-coal-slurry furnace
CN205640978U (en) Energy -conserving combustion system of nitrogen oxide zero release oxygen boosting
CN201944842U (en) Oxygen-enriched combustion-supporting device applied to fuel gas with low heating value
CN201429077Y (en) Water-coal-slurry burner nozzle
CN2881359Y (en) Oxygen enriched powdered coal burner
CN211876713U (en) Local full oxygen boosting calcining device of rotary cement kiln
CN201180983Y (en) Self-adapting ignition combustion device of monotube boiler
CN203784939U (en) Oxygen-enriched micro oil staged combustion device
CN203718767U (en) Oil/gas saving ignition stable-combustion low-nitrogen swirl pulverized coal burner
CN102607286A (en) Molten salt furnace afterheat power-generation and combustion comprehensive utilizing system
CN201672511U (en) Pulverized coal burner
CN111288792A (en) Partial full oxygen-enriched calcining device and process for rotary cement kiln
CN207555603U (en) For the bleeding and energy saving spray gun of Industrial Stoves
CN206176355U (en) Pulverized coal boiler's oxygen boosting combustion system
CN203190442U (en) Oxygen enrichment combustion-supporting energy-saving device of ceramic kiln
CN201159452Y (en) Self-adapting ignition combustor of direct current boiler
CN202371702U (en) Boiler ash recovery after-combustion reutilization energy saving and emission reduction system
CN205782864U (en) A kind of low-BTU gas efficient burning boiler
CN203533549U (en) Micro-oil ignition and oxygen adding burner
CN215951420U (en) Oxygen-enriched combustion system of counter-flow rotary kiln
CN211823873U (en) Crude tunnel kiln waste gas recovery system
CN203586260U (en) Combustion-supporting device
CN218673174U (en) Shuttle kiln flue gas waste heat recovery utilizes system

Legal Events

Date Code Title Description
GR01 Patent grant
GR01 Patent grant