CN203079321U - Powder particle delivery device - Google Patents

Powder particle delivery device Download PDF

Info

Publication number
CN203079321U
CN203079321U CN 201320090906 CN201320090906U CN203079321U CN 203079321 U CN203079321 U CN 203079321U CN 201320090906 CN201320090906 CN 201320090906 CN 201320090906 U CN201320090906 U CN 201320090906U CN 203079321 U CN203079321 U CN 203079321U
Authority
CN
China
Prior art keywords
pipe
powder
winding
jar
pulvis
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
CN 201320090906
Other languages
Chinese (zh)
Inventor
周涛
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.)
CISDI Engineering Co Ltd
Original Assignee
CISDI 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 CISDI Engineering Co Ltd filed Critical CISDI Engineering Co Ltd
Priority to CN 201320090906 priority Critical patent/CN203079321U/en
Application granted granted Critical
Publication of CN203079321U publication Critical patent/CN203079321U/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Images

Landscapes

  • Air Transport Of Granular Materials (AREA)

Abstract

The utility model discloses a powder particle delivery device. The powder particle delivery device comprises a powder storage bin, particle materials of the powder storage bin are connected with the top inlet end of an injecting tank by a discharge pipe, the bottom particle material outlet end of the injecting tank is connected with a powder delivery pipe by a powder regulating valve, the powder particle delivery device is characterized in that the injecting tank is connected with an injecting tank pressurizing pipe and an injecting tank depressurizing pipe, an injecting tank pressure meter is arranged in the injecting tank, and a delivery pipe pressure meter is arranged on the powder delivery pipe, and a delivery riser pipe blowdown pipe is arranged at the bottom of the rising section of the powder delivery pipe. The powder particle delivery device has the characteristics of being capable of controlling the injection gas with small flow, smooth to deliver, preventing the plugging of pipeline, and the like, and the delivery stability can be greatly improved.

Description

A kind of pulvis particle transport device
Technical field
The utility model relates to the Dual-Phrase Distribution of Gas olid conveying technology of material, relates in particular to a kind of pulvis particle transport device.
Background technology
In commercial production, carry for the powder solid material being carried out continuous short distance, tend to make it become fluidized solids with characteristic of fluid with falling the fluidised method of powder, with gas gas is carried then.In the existing desulfurizing iron injection system, generally adopt single-spray particle magnesium or composite blowing technology, in the molten iron treating process, the pulvis discharging rate stabilization that requires injection system to carry just can reach good desulfurized effect, there is following shortcoming in existing pulvis particle transport device: 1, feed is inhomogeneous, influences desulfurized effect; 2, air consumption is big, the energy consumption height; 3, stop up easily, cause the molten iron splash.
The utility model content
The purpose of this utility model is to provide a kind of can realize the stable pulvis particle transport device of carrying of pulvis granule materials.
The purpose of this utility model is achieved through the following technical solutions: a kind of pulvis particle transport device, comprise powder-storage bin, the granule materials of described powder-storage bin links to each other by the top inlet end of discharge duct with the winding-up jar, the bottom granule materials exit end of winding-up jar links to each other with the pulvis delivery pipe by the powder control cock, it is characterized in that: be connected with winding-up jar pressurising pipe and winding-up jar relief tube on the winding-up jar, in the winding-up jar injection tank pressure table is installed, the line pressure table is installed on the pulvis delivery pipe.
Further, the bottom of described pulvis delivery pipe is provided with and carries the ascending pipe blowdown pipe.
Further, a described winding-up jar pressurising pipe is provided with pressurising pipe control cock, according to the signal of injection tank pressure table and line pressure table feedback pressurising pipe control cock is regulated.
Further, described a kind of pulvis particle transport device, described powder control cock is a kind of valve of variable throat.
Principle of work of the present utility model is as follows: at first a winding-up jar blowdown valve is in open state, open discharge valve, material in the powder-storage bin enters the winding-up jar through discharge duct, when the material in the winding-up jar reaches the appointment material level, close discharge valve and blowdown valve, open the equalizer valve in the pressurising pipeline, pressure controller is regulated a winding-up jar equalizer valve according to the force value of injection tank pressure table and pulvis line pressure table output, makes pressure in the winding-up jar less times greater than (about 0.1~1kg/cm 2) the pulvis line pressure.After pressure satisfies specified requirements, open the powder control cock a winding-up jar interior pulvis is flowed out from the bottom, open delivery pipe ascent stage blowdown pipe valve simultaneously, pulvis is exported via spray gun at last.The aperture of the powder control cock by regulating the outlet of winding-up pot bottom is to guarantee to enter pulvis in the winding-up pipeline in the safe range that thin strength is carried.
The utility model not only can effectively utilize coke oven flue gas waste heat and ascending pipe coal gas waste heat to realize the drying of coal simultaneously, also reduced the ammoniacal liquor consumption that is used for the raw coke oven gas cooling in the bridge tube simultaneously, provide an effective way for further realizing the coal chemical enterprise synthetic energy-saving discharge-reducing.
Description of drawings
Fig. 1 is a structural representation of the present utility model.
Among the figure, 1 be powder-storage bin, 2 for winding-up jar, 3 for pressure controller, 4 for the powder control cock, 5 for discharge duct, 6 for the discharge duct valve, 7 for a winding-up jar pressurising pipe, 8 for pressurising pipe control cock, 9 for a winding-up jar relief tube, 10 for the relief tube shutoff valve, 11 for pulvis delivery pipe, 12 for carrying ascending pipe blowdown pipe, 13 to be hot-metal bottle for line pressure table, 16 for injection tank pressure table, 15 for spray gun, 14.
The specific embodiment
Below in conjunction with the drawings and specific embodiments the utility model is described in further detail.
As shown in Figure 1, the pulvis material of powder-storage bin 1 links to each other by the top inlet end of discharge duct 5 with winding-up jar 2, the bottom pulvis material outlet end of winding-up jar 2 links to each other with pulvis delivery pipe 11 by powder control cock 4, winding-up jar pressurising pipe 7 links to each other with winding-up jar 2, winding-up jar relief tube 9 links to each other with winding-up jar 2, in the winding-up jar injection tank pressure table 14 is installed, the pulvis delivery pipe is equipped with line pressure table 15.Described 11 ascent stages of pulvis delivery pipe bottom is provided with carries ascending pipe blowdown pipe 12.A described winding-up jar pressurising pipe 7 is provided with pressurising pipe control cock 8, and its control cock is regulated to pressure controller 3 according to the signal of injection tank pressure table 14 and line pressure table 15 feedback.
During work, at first a winding-up jar blowdown valve is in open state, open discharge valve, material in the powder-storage bin enters the winding-up jar through discharge duct, when the material in the winding-up jar reaches the appointment material level, close discharge valve and blowdown valve, open the equalizer valve in the pressurising pipeline, pressure controller is regulated a winding-up jar equalizer valve according to the force value of injection tank pressure table and pulvis line pressure table output, makes pressure in the winding-up jar less times greater than about 0.1~1kg/cm 2The pulvis line pressure.After pressure satisfies specified requirements, open the powder control cock a winding-up jar interior pulvis is flowed out from the bottom, open delivery pipe ascent stage blowdown pipe valve simultaneously, pulvis is exported via spray gun at last.The aperture of the powder control cock by regulating the outlet of winding-up pot bottom, control enter pulvis in the winding-up pipeline in the safe range that thin strength is carried.
Explanation is at last, above embodiment is only unrestricted in order to the explanation the technical solution of the utility model, although the utility model is had been described in detail with reference to preferred embodiment, those of ordinary skill in the art is to be understood that, can make amendment or be equal to replacement the technical solution of the utility model, and not breaking away from the aim and the scope of technical solutions of the utility model, it all should be encompassed in the middle of the claim scope of the present utility model.

Claims (3)

1. pulvis particle transport device, comprise powder-storage bin, the granule materials of described powder-storage bin links to each other by the top inlet end of discharge duct with the winding-up jar, the bottom granule materials exit end of winding-up jar links to each other with the pulvis delivery pipe by the powder control cock, it is characterized in that: be connected with winding-up jar pressurising pipe and winding-up jar relief tube on the winding-up jar, in the winding-up jar injection tank pressure table is installed, the line pressure table is installed on the pulvis delivery pipe.
2. a kind of pulvis particle transport device according to claim 1 is characterized in that: the bottom of described pulvis delivery pipe is provided with carries the ascending pipe blowdown pipe.
3. a kind of pulvis particle transport device according to claim 1 and 2 is characterized in that: a described winding-up jar pressurising pipe is provided with pressurising pipe control cock, according to the signal of injection tank pressure table and line pressure table feedback pressurising pipe control cock is regulated.
CN 201320090906 2013-02-28 2013-02-28 Powder particle delivery device Expired - Lifetime CN203079321U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN 201320090906 CN203079321U (en) 2013-02-28 2013-02-28 Powder particle delivery device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN 201320090906 CN203079321U (en) 2013-02-28 2013-02-28 Powder particle delivery device

Publications (1)

Publication Number Publication Date
CN203079321U true CN203079321U (en) 2013-07-24

Family

ID=48825179

Family Applications (1)

Application Number Title Priority Date Filing Date
CN 201320090906 Expired - Lifetime CN203079321U (en) 2013-02-28 2013-02-28 Powder particle delivery device

Country Status (1)

Country Link
CN (1) CN203079321U (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103771139A (en) * 2014-02-11 2014-05-07 江苏沙钢集团有限公司 Dense-phase pneumatic conveying system and technology for continuous pulverized coal feeding of blast furnace
US9670559B2 (en) * 2015-07-06 2017-06-06 National Cheng Kung University Method of adding high vapor pressure magnesium to steel liquid and apparatus for performing the method
CN108408414A (en) * 2018-03-19 2018-08-17 中冶华天南京工程技术有限公司 Novel powder material and the uniform transport system of tank
CN111703897A (en) * 2020-05-22 2020-09-25 山东科洋工控自动化有限公司 Automatic control device, system and control method for unloading of powder tank truck

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103771139A (en) * 2014-02-11 2014-05-07 江苏沙钢集团有限公司 Dense-phase pneumatic conveying system and technology for continuous pulverized coal feeding of blast furnace
CN103771139B (en) * 2014-02-11 2016-01-06 江苏沙钢集团有限公司 A kind of blast-furnace coal powder continuous-feeding dense phase pneumatic conveying system and technique
US9670559B2 (en) * 2015-07-06 2017-06-06 National Cheng Kung University Method of adding high vapor pressure magnesium to steel liquid and apparatus for performing the method
CN108408414A (en) * 2018-03-19 2018-08-17 中冶华天南京工程技术有限公司 Novel powder material and the uniform transport system of tank
CN108408414B (en) * 2018-03-19 2020-04-28 中冶华天南京工程技术有限公司 Novel powder material tank-combining uniform conveying system
CN111703897A (en) * 2020-05-22 2020-09-25 山东科洋工控自动化有限公司 Automatic control device, system and control method for unloading of powder tank truck

Similar Documents

Publication Publication Date Title
CN203079321U (en) Powder particle delivery device
CN108674995B (en) High-pressure dilute-phase small-material-quantity feeding device and control method
CN103662842B (en) Continuous charging system
CN202329140U (en) Bellow bypass exhausting system below ignition furnace of sintering machine
CN203855164U (en) Pulverized coal pneumatic conveyor
CN107619895A (en) A kind of device of pulverized coal injection in blast furnace
CN103896334B (en) Except the continuous feeding of scar sand and the Titanium Dioxide Produced by Chloride Procedure process units with it
CN204644271U (en) For the spiral-pulsed the mixture of airstream and strength feeder of mobile biomass pyrolysis
CN103964495A (en) Large fluidizing chlorination furnace and gas distributor thereof
CN201842858U (en) Multiple materials adding regulating device for RH (relative humidity) dry-type vacuum-pumping system
CN203648498U (en) Balanced flow proportion dosing device
CN212687907U (en) Lime slurry preparation system for waste incineration
CN203237785U (en) Pneumatic conveying throat pipe
CN102021352B (en) Apparatus for preparing high-porosity titanium sponge
CN202272507U (en) Long-distance and high-output continuous delivery pump
CN205008230U (en) Coal powder injection blowback filter
CN204329539U (en) A kind of hot-air drying unit
CN204369822U (en) A kind of energy saver of fixed bed coal gas producer steam
CN202808861U (en) Powder injecting and automatic-fluidizing device
CN208560956U (en) A kind of equipment of powder material Dense Phase Pneumatic Conveying
CN101968300A (en) Boiling drying device
CN202277918U (en) Device for liquid spraying
CN205771992U (en) Colophonium carries negative pressure system continuously
CN204588107U (en) A kind of low discharge Pneumatic feeding device for gasification furnace feed
CN203558849U (en) Sulphur storage tail gas and liquid sulphur degassing comprehensive treatment system

Legal Events

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

Granted publication date: 20130724

CX01 Expiry of patent term