CN201625500U - Calcium spraying flue gas desulfurization device in limestone furnace - Google Patents

Calcium spraying flue gas desulfurization device in limestone furnace Download PDF

Info

Publication number
CN201625500U
CN201625500U CN2010201512625U CN201020151262U CN201625500U CN 201625500 U CN201625500 U CN 201625500U CN 2010201512625 U CN2010201512625 U CN 2010201512625U CN 201020151262 U CN201020151262 U CN 201020151262U CN 201625500 U CN201625500 U CN 201625500U
Authority
CN
China
Prior art keywords
storage tank
feeder
flue gas
type
screw
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.)
Expired - Lifetime
Application number
CN2010201512625U
Other languages
Chinese (zh)
Inventor
刘国君
朱跃武
李虹琳
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.)
TIANJIN TNPL ENVIRONMENTAL ENGINEERING Co Ltd
Original Assignee
TIANJIN TNPL 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 TIANJIN TNPL ENVIRONMENTAL ENGINEERING Co Ltd filed Critical TIANJIN TNPL ENVIRONMENTAL ENGINEERING Co Ltd
Priority to CN2010201512625U priority Critical patent/CN201625500U/en
Application granted granted Critical
Publication of CN201625500U publication Critical patent/CN201625500U/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Landscapes

  • Treating Waste Gases (AREA)

Abstract

The utility model relates to a calcium spraying flue gas desulfurization device in a limestone furnace, and the device is a device which can continuously spray material; the calcium spraying flue gas desulfurization device is provided with a material storage tank, the upper part of the material storage tank is provide with a high-level material meter and a round top material inlet valve, the lower part thereof is provided with a low-level material meter, the material outlet is sequentially connected with a quantitative spiral feeding machine and a spraying pump, the upper part of the material inlet valve of the material storage tank is connected with a material receiving cabin, the material storage tank is communicated with the material cabin and a spiral conveying machine nose by a connecting pipe, a communication pipe is provided with two balance valves which have operating and discharging balanced functions; the material storage tank with the spraying operating state is communicated with the spiral conveying machine nose, and the material storage tank with the material feeding state is communicated with the material cabin; when in operation, the low material level of the material storage tank alarms, the material feeding valve and the balance valves are changed into the material feeding state to recharge the material to the material storage tank; in the utility model, single material storage tank feeding mode is adopted, the equipment height is effectively reduced, the system is simplified, equipment investment is reduced and the material feeding effect of the traditional double tanks can be achieved at the meantime.

Description

Lime stone in-furnace calcium spraying flue gas desulfur device
Technical field
The utility model belongs to the desulfurating dust-removing equipment field, especially a kind of lime stone in-furnace calcium spraying flue gas desulfur device.
Background technology
Lime stone in-furnace calcium spraying flue gas desulfur device mainly is applicable to the inner flue gas of the stove desulfurization of coal furnace power plant boiler.The main task of this device is to finish mass transport, metering, powder sending quantity adjusting and stokehold to spray, thereby agstone calcination in stove is decomposed, and utilizes the CaO of generation and the SO in the inner flue gas of the stove 2React the realization desulfuration in furnace.This device mainly is made of material-transporting system and air-transport system, material-transporting system mainly comprises two storage tank, screw(-type) feeder and the jet pumps vertically installed, the inside of these two storage tanks is connected, a feed bin (ash-storing bin) is installed in the upper end of last storage tank, the discharging opening place of following storage tank connects screw(-type) feeder, the outlet of screw(-type) feeder connects jet pump, and jet pump is connected with air-transport system.Owing on the last storage tank high-order material meter and dome inlet valve have been installed, low level material meter and dome inlet valve have been installed on the following storage tank, therefore under the effect of high position material meter, low level material meter and two dome inlet valves, agstone through feed bin, storage tank, screw(-type) feeder and jet pump after, can be injected under the effect of air-transport system advance in the boiler and carry out desulfurization.
In use there is following defective in this desulfurizer: 1, owing to not having the installation material material level to put supervising device on the storage tank down, need lean on time control the closing and opening of dome inlet valve of storage tank down when adopting two jars of chargings, therefore the control point is many, control accuracy is low, causes easily that the feeding error is big, transfer efficiency is low; 2, owing to the storage tanks that adopt two vertically to install, so the equipment whole height is higher, and it is bigger to take up room, and during installation factory building is had relatively high expectations, and is not suitable for installing and using in highly shorter occasion; 3,, cause and install and the equal inconvenience of maintenance because material-transporting system and connected feed bin height are higher.
The utility model content
The purpose of this utility model is to overcome the deficiencies in the prior art, provides a kind of reasonable in design, can reduce the equipment whole height, makes things convenient for installation and maintenance, and charging precision height can improve the lime stone in-furnace calcium spraying flue gas desulfur device of agstone transfer efficiency.
The utility model solves its technical problem and is achieved through the following technical solutions:
A kind of lime stone in-furnace calcium spraying flue gas desulfur device, comprise material-transporting system and air-transport system, material-transporting system comprises screw(-type) feeder, jet pump and the storage tank that is connected with feed bin, it is characterized in that: the storage tank in the material-transporting system is one, high-order material meter and dome inlet valve are installed in the top of this storage tank, dome inlet valve top connects feed bin, and low level material meter is installed in the bottom of storage tank, and the discharging opening of storage tank connects screw(-type) feeder and jet pump successively; The top of storage tank is communicated with a balance pipe that vertically is provided with by a tube connector, the upper end of this balance pipe connects feed bin, the lower end connects screw(-type) feeder, in that balanced valve on is installed on the balance pipe between feed bin and the tube connector, balanced valve once is installed on the balance pipe between screw(-type) feeder and the tube connector.
And described air-transport system comprises roots blower and conveyance conduit.
And described screw(-type) feeder is quantitative screw(-type) feeder.
Advantage of the present utility model and beneficial effect are:
1, the storage tank in this desulfurizer has only one, high-order material meter and the score of low level material are not installed in the upper and lower of storage tank, therefore high and low position material meter can be monitored constantly to the height of materials in the tank body, guarantee the accuracy of charging, reduce the error of charging, improve the transfer efficiency of material.
2, single jar of charging in this desulfurizer is that the pressure in the storage tank is discharged charging again from balance pipe earlier, because screw(-type) feeder can be sealed the pressure in the conveying, so to carrying not influence, solved the problem that the decompression influence is carried in carrying.Reduced though this device is compared equipment with legacy equipment, still can reach same desulfurization and dedusting effect, and production cost is significantly reduced.
3, the material-transporting system of this desulfurizer makes single jar structure into by two jar structures of vertical setting, makes the whole height of this device greatly reduce, and the factory building height limited degree reduces, and has increased the scope of application of this device.
4, after this desulfurizer whole height reduces, not only be convenient to the equipment installation and maintenance, and make feed bin arrangement convenience in the boiler room.
5, the utility model is a kind of reasonable in design, simple in structure, installation and maintenance lime stone in-furnace calcium spraying flue gas desulfur devices easily, this device adopts single jar of feeding manner, has improved the charging precision, has reduced and produced the effect that drops into and can reach the charging of traditional double jar equally.
Description of drawings
Fig. 1 is a front view of the present utility model.
The specific embodiment
The utility model is described in further detail below by specific embodiment, and following examples are descriptive, is not determinate, can not limit protection domain of the present utility model with this.
A kind of lime stone in-furnace calcium spraying flue gas desulfur device, mainly constitute by material-transporting system and air-transport system, air-transport system comprises roots blower 1 and conveyance conduit 2, material-transporting system comprises screw(-type) feeder 12, jet pump 13 and the storage tank 9 that is connected with feed bin 3, and this screw(-type) feeder is quantitative screw(-type) feeder.
Innovative point of the present utility model is: the storage tank in the material-transporting system is one, high-order material meter 4, expansion joint and dome inlet valve 5 are installed in the top of this storage tank, in the bottom of storage tank low level material meter 10 is installed, the discharging opening of this storage tank connects screw(-type) feeder and jet pump successively.Conveyance conduit outlet in the air-transport system is positioned at the jet pump exit, therefore agstone can be sprayed in the boiler.
The top tank body of storage tank (between high position material meter and low level material meter) is communicated with a balance pipe 11 that vertically is provided with by a tube connector 7, and the top of this balance pipe is communicated with feed bin, and balanced valve 6 on is being installed on the balance pipe between feed bin and the tube connector; The below of balance pipe is communicated with screw(-type) feeder, and balanced valve 8 once is installed on the balance pipe between screw(-type) feeder and the tube connector.Should go up balanced valve and play two kinds of balanced actions that move with the blanking two states with following balanced valve.Spray running status storage tank and screw(-type) feeder (helical feed head) UNICOM, when feed state storage tank and feed bin UNICOM.Be in operation when the low material level of storage tank is reported to the police, inlet valve and balanced valve are changed to feed state and fill it up with material to storage tank.
The course of work of the present utility model is:
1, go up balanced valve and open, balanced valve cuts out at present together;
2, dome inlet valve sealing ring rushes down pressure, and inlet valve is opened (charging) simultaneously;
3, when high position material meter sends full material signal, close inlet valve sealing ring pressurising simultaneously;
4, go up balanced valve and close, balanced valve is opened at present together;
5, open air-transport system (roots blower etc.), treat steady air current after, open screw(-type) feeder.Situation according to sulfur-bearing in the flue dust, adjust feeding coal, realize dosing, material (agstone) vertically falls to entering screw(-type) feeder by storage tank, along continuous straight runs is pushed ahead under the effect of screw(-type) feeder, under the effect of jet pump and roots blower, be ejected in the boiler at last, carry out desulfurization and dedusting;
6, send when lacking the material signal when low level material meter, repeat 1~4 and realize carrying continuously.

Claims (3)

1. lime stone in-furnace calcium spraying flue gas desulfur device, comprise material-transporting system and air-transport system, material-transporting system comprises screw(-type) feeder, jet pump and the storage tank that is connected with feed bin, it is characterized in that: the storage tank in the material-transporting system is one, high-order material meter and dome inlet valve are installed in the top of this storage tank, dome inlet valve top connects feed bin, and low level material meter is installed in the bottom of storage tank, and the discharging opening of storage tank connects screw(-type) feeder and jet pump successively; The top of storage tank is communicated with a balance pipe that vertically is provided with by a tube connector, the upper end of this balance pipe connects feed bin, the lower end connects screw(-type) feeder, in that balanced valve on is installed on the balance pipe between feed bin and the tube connector, balanced valve once is installed on the balance pipe between screw(-type) feeder and the tube connector.
2. lime stone in-furnace calcium spraying flue gas desulfur device according to claim 1, it is characterized in that: described air-transport system comprises roots blower and conveyance conduit.
3. lime stone in-furnace calcium spraying flue gas desulfur device according to claim 1 is characterized in that: described screw(-type) feeder is quantitative screw(-type) feeder.
CN2010201512625U 2010-04-07 2010-04-07 Calcium spraying flue gas desulfurization device in limestone furnace Expired - Lifetime CN201625500U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN2010201512625U CN201625500U (en) 2010-04-07 2010-04-07 Calcium spraying flue gas desulfurization device in limestone furnace

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN2010201512625U CN201625500U (en) 2010-04-07 2010-04-07 Calcium spraying flue gas desulfurization device in limestone furnace

Publications (1)

Publication Number Publication Date
CN201625500U true CN201625500U (en) 2010-11-10

Family

ID=43056882

Family Applications (1)

Application Number Title Priority Date Filing Date
CN2010201512625U Expired - Lifetime CN201625500U (en) 2010-04-07 2010-04-07 Calcium spraying flue gas desulfurization device in limestone furnace

Country Status (1)

Country Link
CN (1) CN201625500U (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105752693A (en) * 2016-02-29 2016-07-13 河南丰博自动化有限公司 Quantified powder feeding system
CN109250506A (en) * 2018-09-13 2019-01-22 常州泰聚环保科技有限公司 A kind of material-transporting system preventing material plate knot

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105752693A (en) * 2016-02-29 2016-07-13 河南丰博自动化有限公司 Quantified powder feeding system
CN105752693B (en) * 2016-02-29 2018-06-05 河南丰博自动化有限公司 A kind of given quantity feeding system
CN109250506A (en) * 2018-09-13 2019-01-22 常州泰聚环保科技有限公司 A kind of material-transporting system preventing material plate knot

Similar Documents

Publication Publication Date Title
CN102974211A (en) Circulating fluidized bed boiler in-furnace desulfurization device
CN110053887A (en) A kind of cement plant powder denitrfying agent conveying device and its application method
CN201302374Y (en) Selective desulfurization device for flue gas of sintering machine head
CN201625500U (en) Calcium spraying flue gas desulfurization device in limestone furnace
CN103816795A (en) Semi-dry process desulfurization dust-removing technique and device
CN203173991U (en) Sealed-tank quicklime slaker
CN201168568Y (en) Water-lime powder combined spray gun
CN203199676U (en) Bunched-tank rotary feeding injection pump
CN209612628U (en) A kind of lime slaking slurrying injection apparatus of semi-dry desulphurization
CN103566751A (en) Fluidized bed boiler desulfurization method and device
CN201372128Y (en) Delivery device for preventing bridging of powder
CN2657757Y (en) Spray device of active carbon for purifying smoke of garbage incineration
CN204017657U (en) A kind of sintering device flue gas wet desulphurization equipment
CN203512422U (en) Sintering flue gas desulfurized fly ash bin
CN2803532Y (en) Pneumatic solid particles spray gun
CN202893181U (en) Desulphurization device in circulating fluidized bed boiler
CN202654938U (en) Pneumatic conveying dry-powder direct feeding desulfurizing system
CN210385465U (en) Dry method tower slaked lime and active carbon injection device
CN208553733U (en) A kind of system that base reagent removes sulfur trioxide in flue gas
CN208372795U (en) A kind of double method depickling reaction units of a tower
CN215138607U (en) A spout calcium system in stove for boiler flue gas desulfurization
CN102125798A (en) Dry numerical control circulating vulcanization desulfurization device
CN205073878U (en) Exhaust gas treatment system
CN215196302U (en) Desulfurization ash unloading disturbance device
CN205341423U (en) Automatic cleaning device at bottom of circulating fluidized bed flue gas desulfurization reaction tata

Legal Events

Date Code Title Description
C14 Grant of patent or utility model
GR01 Patent grant
CX01 Expiry of patent term

Granted publication date: 20101110

CX01 Expiry of patent term