CN202849472U - Oxygen-enriched dry gas supply device - Google Patents

Oxygen-enriched dry gas supply device Download PDF

Info

Publication number
CN202849472U
CN202849472U CN201220448792.5U CN201220448792U CN202849472U CN 202849472 U CN202849472 U CN 202849472U CN 201220448792 U CN201220448792 U CN 201220448792U CN 202849472 U CN202849472 U CN 202849472U
Authority
CN
China
Prior art keywords
oxygen
cooler
blast furnace
dry gas
air
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
CN201220448792.5U
Other languages
Chinese (zh)
Inventor
李东林
郎治
王华金
苏为民
马光俊
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.)
Individual
Original Assignee
Individual
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 Individual filed Critical Individual
Priority to CN201220448792.5U priority Critical patent/CN202849472U/en
Application granted granted Critical
Publication of CN202849472U publication Critical patent/CN202849472U/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Images

Abstract

The utility model relates to the technical field of blast furnace iron-making process, and provides an oxygen-enriched dry gas supply device suitable for a blast furnace iron-making procedure. The oxygen-enriched dry gas supply device is characterized in that a blast furnace blower is connected with a pre-cooler, the pre-cooler is connected with an air cooler, the air cooler is connected with a PSA (pressure swing adsorption) oxygen generation device which is connected with the pre-cooler, and the pre-cooler is connected with a hot blast heater. The oxygen-enriched dry gas supply device disclosed by the utility model fully utilizes devices in the traditional blast furnace iron-making smelting process, directly produces oxygen-enriched dry gas through PSA by gas pressurized by a blast furnace blower outlet and has the characteristics of low device investment and low operation energy consumption.

Description

A kind of oxygen enrichment dry gas feeding mechanism for blast furnace ironmaking
Technical field
The utility model relates to the blast furnace iron-making process technical field, is specifically related to a kind of feeding mechanism of pressurized air directly being made the oxygen enrichment dry gas that can be used for blast furnace ironmaking.
Background technology
In blast furnace iron-making process, oxygen enriched blast technology and dehumidified blast technology are the strengthening smelting technology of comparatively widespread use.Wherein, oxygen enriched blast mainly is to add industrial oxygen to improve oxygen level in the air blast when air blast, makes oxygen-enriched content in the gas 〉=21%, improves combustion intensity and cupola well tuyere zone temperature of combustion, thereby improves furnace processor and reduce coke ratio.Dehumidified blast then is by removing the moisture in the blast furnace blast, make the humidity of the combustion air that enters blast furnace be reduced to the desired numerical value of optimum operation and keep stable, thereby play the effect that improves dry-air blast temperature, stable furnace condition, increase coal powder blowing amount, reduces coke ratio.
At present, common oxygen enrichment adding method mainly is that independently PSA(pressure-variable adsorption is set before blast furnace blowing engine in the oxygen enriched blast technology) or the VPSA(Vacuum Pressure Swing Adsorption) oxygenerator, and before blast furnace blowing engine, add made oxygen enrichment in the import airduct, perhaps, independently PSA or the made oxygen enrichment of the VPSA oxygenerator cold-air duct between blast furnace blowing engine and snorting valve after the oxygen compressor pressurization is added.
CN03117856.1, denomination of invention discloses the compression-expansion Deep Cooling Method of a kind of PSA of employing or VPSA absorption method and normal pressure output oxygen and the membrane separation process air separation facility provides oxygen enrichment for blast furnace ironmaking oxygen-enriched coal spray technique the oxygen that supplies for the Chinese invention patent of " the confession oxygen of blast furnace ironmaking oxygen-enriched coal spray ".This technical scheme mainly is: be added in during oxygen supply before the blast furnace blowing engine suction port together to be sucked by blast furnace blowing engine with air and be mixed into the required oxygen enrichment of oxygen enriched blast coal injection iron-smelting process and send into blast furnace, or after pressurization, send in the blast main of blast furnace blowing engine outlet with the gas blower pressurization after air mixed send into blast furnace after evenly.Still there is following shortcoming in this confession oxygen: owing to adopt air compressor machine or vacuum unit in the preparation oxic process, it is larger that oxygen enrichment prepares energy consumption, and as adding the mode of oxygen enrichment behind the employing blast furnace blowing engine, then also need increase oxygen compressor boosts, energy consumption and investment also need further to improve, and complete assembly system operation energy consumption is high, occupation area of equipment is large, and investment is large.
And with regard to dehumidified blast, the current method that then mainly adopts gas blower suction side cooling dehumidification, this dehumidification method need increase freezing unit, and investment is high, and operation energy consumption is higher.
CN200910103264.9, denomination of invention discloses a kind of back dehumidifying device of stove blower for the Chinese invention patent of " a kind of back dehumidifying device of stove blower ", its technical scheme mainly is: by dehumidifying device being placed on blast furnace blowing engine outlet, the air of the High Temperature High Pressure of blast furnace blowing engine outlet is carried out precooling, dehumidification and backheat successively.But this technical scheme does not take full advantage of blast furnace blowing engine, still air directly can not be made the oxygen enrichment dry gas that can be used for blast furnace ironmaking, but need to satisfy by the mode of external interpolation oxygen enrichment the requirement of the oxygen enrichment dry gas that can be used for blast furnace ironmaking.
CN98228550.7, the utility model patent that name is called " a kind of oxygen-enriched combustion device for glass bead kiln " discloses a kind of oxygen-enriched combustion device for glass bead kiln, by gas blower, oxygen-enriched generator, water-ring vacuum pump, air water separator, dehumidification case, gas-water separation case, booster fan, reversing system, preheater, nozzle, air purifier, airduct be flexible coupling, drain bucket forms, utilize membrane oxygen enrichment technology, 28~35%O is provided 2The oxygen-rich air of content is with Sweet natural gas mixed firing.This technical scheme only is only applicable to specific glass bead kiln, adopt membrane oxygen enrichment technology, send into air by gas blower, need simultaneously to provide in conjunction with water-ring vacuum pump the enough pressure reduction of embrane method oxygen enrichment processed, and by booster fan to made oxygen enrichment supercharging to satisfy the pressure of subsequent request.Therefore, still there is the shortcoming that the power-equipment investment is large, energy consumption is high in this oxygen-enriched burning device, and is not suitable for blast furnace ironmaking.
Therefore, consider whole blast furnace ironmaking oxygen enriched blast air feed flow process, and prepare the angle of energy consumption and dehumidification energy consumption from reducing oxygen enrichment, be necessary to set up the new blast furnace ironmaking oxygen enrichment dry gas supply technique in conjunction with dehumidification usefulness, to take full advantage of existing device in the existing blast furnace iron-making process, under the prerequisite that guarantees oxygen-enriched content, reduce cost and running cost, save energy consumption.
The utility model content
The utility model is intended to overcome the shortcoming of above-mentioned prior art, and a kind of oxygen enrichment dry gas feeding mechanism that adapts with blast furnace ironmaking strengthening smelting process is provided.This device takes full advantage of the equipment in the existing blast furnace ironmaking smelting technology, will be through the air after the blast furnace blowing engine outlet supercharging, directly prepare the oxygen enrichment dry gas through PSA oxygen processed unit, having changed needs external interpolation oxygen enrichment to produce the oxygen enrichment dry gas in the prior art, possess the characteristics that facility investment is low, operation energy consumption is low.
For solving above technical problem, technical scheme provided by the utility model is as follows:
A kind of oxygen enrichment dry gas feeding mechanism for blast furnace ironmaking, comprise blast furnace blowing engine, pre-cooler, air cooler, PSA oxygen processed unit and hotblast stove, it is characterized in that: described blast furnace blowing engine connects pre-cooler, pre-cooler connects air cooler, air cooler connects PSA oxygen processed unit, PSA oxygen processed unit connects pre-cooler, and pre-cooler connects hotblast stove; Air after the blast furnace blowing engine supercharging cools through pre-cooler, air cooler, enters PSA oxygen processed unit again and obtains the oxygen enrichment dry gas, and gained oxygen enrichment dry gas is got back to pre-cooler and heated up, and then enters hotblast stove and is sent to blast furnace as combustion-supporting.
Described oxygen enrichment dry gas feeding mechanism also comprises air water separator, and described pre-cooler connects air cooler, and air cooler connects air water separator, and air water separator connects PSA oxygen processed unit, and PSA oxygen processed unit connects pre-cooler; Air after the blast furnace blowing engine supercharging cools through pre-cooler, air cooler, and the gas after the cooling is deviate from the moisture in the gas in air water separator, enters PSA oxygen processed unit again and obtains the oxygen enrichment dry gas.
Described PSA oxygen processed unit adopts a plurality of adsorption towers in parallel, is filled with successively dehydrated adsorbent and oxygen molecular sieve processed in the adsorption tower from bottom to top, with adsorbing and removing minor amount of water and nitrogen.
Described adsorption tower, each adsorption tower operation steps comprise successively absorption, drop pressure, along put, inverse put, flushing, boost pressure, gas product boost.The staggered absorption of a plurality of adsorption towers and regeneration, thus make air be able to dehumidification and be prepared into the oxygen enrichment dry gas.Prepared oxygen enrichment dry gas is compared with the mode that oxygen enrichment is added in the outside, and its oxygen level is greatly enhanced, and is convenient to adjusting, stability height.
The oxygen level of described oxygen enrichment dry gas by volume per-cent greater than 21%, dew-point temperature below-10 ℃, humidity is less than 2 g/m 3
The beneficial effects of the utility model are:
1, the utility model device adopts PSA oxygen processed unit to be positioned over after the exit end of blast furnace blowing engine, take full advantage of the elevated pressures of the outlet air that blast furnace blowing engine provides, directly with air pressure-variable adsorption oxygen enrichment processed, make the process simplification of follow-up oxygen enrichment processed, need not to add such as power-equipments such as air compressor machine or vacuum units, PSA is set independently or VPSA oxygen-enriching device processed is compared with at present commonly used, optimized facility investment, significantly reduced the energy consumption of oxygen enrichment preparation process, very effectively reduced the preparation energy consumption of oxygen enrichment dry gas, improve the economy of blast furnace ironmaking device, possessed low facility investment, the characteristics of low operation energy consumption.
2, the utility model adopts the mode that pre-cooler and blast furnace blowing engine are connected with PSA oxygen processed unit.The pre-cooler has here been brought into play following effect: the air of (1) blast furnace blowing engine outlet is lowered the temperature through pre-cooler first, enters air cooler again and again lowers the temperature, to satisfy the processing requirement of PSA; (2) pre-cooler oxygen enrichment dry gas that PSA is made heats up to the oxygen enrichment dry gas as heat-eliminating medium, has effectively utilized the heat of blower export gas, thereby has reached energy-conservation purpose.
3, the utility model adopts pre-cooler to connect air cooler, and the method for air water separator is set behind air cooler, elevated pressures and the temperature of the outlet air that blast furnace blowing engine provides have been utilized well, the air dehumidification is processed be need not to add freezing unit, optimized facility investment, significantly reduced the energy consumption that the air dehumidification is processed, thereby very effectively reduced the preparation energy consumption of oxygen enrichment dry gas, further improve the economy of blast furnace ironmaking device, and formed blast furnace ironmaking oxygen enrichment dry gas supply technique in conjunction with dehumidification usefulness with this.
4, the utility model adopts the PSA oxygen processed unit of a plurality of adsorption tower parallel connections, the staggered absorption of a plurality of adsorption towers and regeneration, and the moisture in the deaerated and nitrogen satisfy the requirement of the oxygen enrichment dry gas of producing high density well.Prepared oxygen enrichment dry gas is compared with the mode that oxygen enrichment is added in the outside, and its oxygen level is greatly enhanced, and is convenient to adjusting, stability height.
Description of drawings
Fig. 1 is the oxygen enrichment dry gas feeding mechanism structure iron of the blast furnace ironmaking implemented according to the utility model content.
Fig. 2 is the oxygen enrichment dry gas feeding mechanism structure iron of the blast furnace ironmaking of the utility model embodiment 2.
Embodiment
Embodiment 1
A kind of oxygen enrichment dry gas feeding mechanism for blast furnace ironmaking, comprise blast furnace blowing engine, pre-cooler, air cooler, PSA oxygen processed unit and hotblast stove, it is characterized in that: described blast furnace blowing engine connects pre-cooler, pre-cooler connects air cooler, air cooler connects PSA oxygen processed unit, PSA oxygen processed unit connects pre-cooler, and pre-cooler connects hotblast stove; Air after the blast furnace blowing engine supercharging cools through pre-cooler, air cooler, enters PSA oxygen processed unit again and obtains the oxygen enrichment dry gas, and gained oxygen enrichment dry gas is got back to pre-cooler and heated up, and then enters hotblast stove and is sent to blast furnace as combustion-supporting.
The gauge pressure pressure of described blast furnace blowing engine outlet air is 0.25MPa.
Described PSA oxygen processed unit adopts a plurality of adsorption towers in parallel, is filled with successively dehydrated adsorbent and oxygen molecular sieve processed in the adsorption tower from bottom to top, with adsorbing and removing minor amount of water and nitrogen.
Described adsorption tower, each adsorption tower operation steps comprise successively absorption, drop pressure, along put, inverse put, flushing, boost pressure, gas product boost.
Air themperature before the described PSA of the entering oxygen processed unit is below 85 ℃.
The atmospheric moisture that enters before the PSA oxygen processed unit is 5~10g/m 3
The dew-point temperature of described oxygen enrichment dry gas is below-10 ℃, and oxygen level is greater than 21%, and humidity is less than 2g/m 3
The utility model takes full advantage of the most important power-equipment of blast furnace---blast furnace blowing engine, not only directly produce the required oxygen of blast-furnace smelting by oxygen enrichment dry gas feeding mechanism described in the utility model, and provide and overcome the required aerodynamic force of blast furnace stock column resistance, need not be with the mode of the adding oxygen enrichment oxygen enrichment dry gas as blast furnace ironmaking.
Embodiment 2
As a same reason, such as embodiment 1
A kind of oxygen enrichment dry gas feeding mechanism for blast furnace ironmaking, comprise blast furnace blowing engine, pre-cooler, air cooler, PSA oxygen processed unit and hotblast stove, it is characterized in that: described blast furnace blowing engine connects pre-cooler by pipeline, pre-cooler connects air cooler, air cooler connects PSA oxygen processed unit, PSA oxygen processed unit connects pre-cooler, and pre-cooler connects hotblast stove; The gauge pressure pressure of described blast furnace blowing engine outlet air is 0.35Mpa, and the air themperature before the described PSA of the entering oxygen processed unit is 85 ℃, and humidity is 10g/m 3, obtaining dew-point temperature and be-10 ℃, oxygen level 23%, humidity are 1.92 g/m 3The oxygen enrichment dry gas, gained oxygen enrichment dry gas is got back to pre-cooler and is heated up, and then enters hotblast stove and is sent to blast furnace as combustion-supporting.
Described oxygen enrichment dry gas feeding mechanism also comprises air water separator, and described pre-cooler connects air cooler, and air cooler connects air water separator, and air water separator connects PSA oxygen processed unit, and PSA oxygen processed unit connects pre-cooler; Air after the blast furnace blowing engine supercharging cools through pre-cooler, air cooler, and the gas after the cooling is deviate from the moisture in the gas in air water separator, enters PSA oxygen processed unit again and obtains the oxygen enrichment dry gas.
Embodiment 3
As a same reason, as aforementioned
A kind of oxygen enrichment dry gas feeding mechanism for blast furnace ironmaking, comprise blast furnace blowing engine, water cooler, air water separator, PSA oxygen processed unit and hotblast stove, it is characterized in that: described blast furnace blowing engine connects pre-cooler by pipeline, pre-cooler connects air cooler, air cooler connects PSA oxygen processed unit, PSA oxygen processed unit connects pre-cooler, and pre-cooler connects hotblast stove; The gauge pressure pressure 0.45Mpa of described blast furnace blowing engine outlet air, the air themperature before the described PSA of the entering oxygen processed unit is 75 ℃, humidity is 8g/m 3, obtaining dew-point temperature and be-20 ℃, oxygen level 22%, humidity are 0.76 g/m 3The oxygen enrichment dry gas, gained oxygen enrichment dry gas is got back to pre-cooler and is heated up, and then enters hotblast stove and is sent to blast furnace as combustion-supporting.
Embodiment 4
As a same reason, as aforementioned
A kind of oxygen enrichment dry gas feeding mechanism for blast furnace ironmaking, comprise blast furnace blowing engine, water cooler, air water separator, PSA oxygen processed unit and hotblast stove, it is characterized in that: described blast furnace blowing engine connects pre-cooler by pipeline, pre-cooler connects air cooler, air cooler connects PSA oxygen processed unit, PSA oxygen processed unit connects pre-cooler, and pre-cooler connects hotblast stove; The gauge pressure pressure 0.58Mpa of described blast furnace blowing engine outlet air, the air themperature before the described PSA of the entering oxygen processed unit is 65 ℃, humidity is 6g/m 3, obtaining dew-point temperature and be-30 ℃, oxygen level 23%, humidity are 0.28 g/m 3The oxygen enrichment dry gas, gained oxygen enrichment dry gas is got back to pre-cooler and is heated up, and then enters hotblast stove and is sent to blast furnace as combustion-supporting.
Embodiment 5
As a same reason, as aforementioned
A kind of oxygen enrichment dry gas feeding mechanism for blast furnace ironmaking, comprise blast furnace blowing engine, water cooler, air water separator, PSA oxygen processed unit and hotblast stove, it is characterized in that: described blast furnace blowing engine connects pre-cooler by pipeline, pre-cooler connects air cooler, air cooler connects PSA oxygen processed unit, PSA oxygen processed unit connects pre-cooler, and pre-cooler connects hotblast stove; The gauge pressure pressure of described blast furnace blowing engine outlet air is 0.75Mpa, and the air themperature before the described PSA of the entering oxygen processed unit is 80 ℃, and humidity is 5g/m 3, obtaining dew-point temperature and be-40 ℃, oxygen level 24%, humidity are 0.09 g/m 3The oxygen enrichment dry gas, gained oxygen enrichment dry gas is got back to pre-cooler and is heated up, and then enters hotblast stove and is sent to blast furnace as combustion-supporting.
The utility model has utilized the elevated pressures of the outlet air that blast furnace blowing engine provides well, make follow-up air dehumidification processing and pressure-variable adsorption oxic process processed all need not to add as freezing unit, air compressor machine, oxygen compressor, the power-equipments such as vacuum pump, thereby with present PSA(or the VPSA of independently arranging commonly used) oxygen-enriching device processed and method of cooling dehumidifying device compare, optimized facility investment, significantly reduced the energy consumption of the processing of air dehumidification and oxic process processed, very effectively reduced the preparation energy consumption of oxygen enrichment dry gas, improved the economy of blast furnace ironmaking device, and form with this and can satisfy simultaneously oxygen enriched blast and dehumidified blast requirement, possess low facility investment, the oxygen enrichment dry gas supply chain of low operation energy consumption characteristics.

Claims (3)

1. oxygen enrichment dry gas feeding mechanism that is used for blast furnace ironmaking, comprise blast furnace blowing engine, pre-cooler, air cooler, PSA oxygen processed unit and hotblast stove, it is characterized in that: described blast furnace blowing engine connects pre-cooler, pre-cooler connects air cooler, air cooler connects PSA oxygen processed unit, PSA oxygen processed unit connects pre-cooler, and pre-cooler connects hotblast stove.
2. a kind of oxygen enrichment dry gas feeding mechanism for blast furnace ironmaking according to claim 1, it is characterized in that: described oxygen enrichment dry gas feeding mechanism also comprises air water separator, described pre-cooler connects air cooler, air cooler connects air water separator, air water separator connects PSA oxygen processed unit, and PSA oxygen processed unit connects pre-cooler.
3. according to claim 1 or 2 described a kind of oxygen enrichment dry gas feeding mechanisms for blast furnace ironmaking, it is characterized in that: described PSA oxygen processed unit, adopt a plurality of adsorption towers in parallel.
CN201220448792.5U 2012-09-05 2012-09-05 Oxygen-enriched dry gas supply device Expired - Lifetime CN202849472U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201220448792.5U CN202849472U (en) 2012-09-05 2012-09-05 Oxygen-enriched dry gas supply device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201220448792.5U CN202849472U (en) 2012-09-05 2012-09-05 Oxygen-enriched dry gas supply device

Publications (1)

Publication Number Publication Date
CN202849472U true CN202849472U (en) 2013-04-03

Family

ID=47980692

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201220448792.5U Expired - Lifetime CN202849472U (en) 2012-09-05 2012-09-05 Oxygen-enriched dry gas supply device

Country Status (1)

Country Link
CN (1) CN202849472U (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102808053A (en) * 2012-09-05 2012-12-05 李东林 Oxygen-rich dry gas supply device for blast furnace iron-making
CN103868346A (en) * 2014-03-17 2014-06-18 济南市平阴县玛钢厂 Oxygen-enriched nitrogen supply system for cupola furnace

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102808053A (en) * 2012-09-05 2012-12-05 李东林 Oxygen-rich dry gas supply device for blast furnace iron-making
CN103868346A (en) * 2014-03-17 2014-06-18 济南市平阴县玛钢厂 Oxygen-enriched nitrogen supply system for cupola furnace

Similar Documents

Publication Publication Date Title
CN104515361A (en) Method for producing liquid carbon dioxide
CN106365123A (en) Single-lobe-pump dual-action medical molecular sieve oxygen generating system and oxygen generating method
CN102808056A (en) Oxygen-enriched dry gas supply process for blast furnace iron-making
CN101526223B (en) Combustion-supporting and energy-saving device capable of using total oxygen and rich oxygen simultaneously in vacuum variable-pressure absorption oxygen generation
CN202849472U (en) Oxygen-enriched dry gas supply device
CN103249464B (en) By the method and apparatus of the fluid of the waste gas production carbon dioxide-enriched of iron and steel industry unit
CN103451340B (en) Device and method thereof for increasing air temperature of hot blast furnace by utilizing air voltage transformation to adsorb oxygen enrichment
CN102826509B (en) Equipment for purifying general hydrogen gas into high-purity hydrogen gas
CN102976291A (en) Variable pressure adsorption nitrogen production equipment and method thereof
CN205730788U (en) A kind of cement kiln tail smoke carbon dioxide upgrading system
CN103868346B (en) Oxygen-enriched nitrogen supply system for cupola furnace
CN201209146Y (en) Low nitrogen blast furnace blower
CN102502513B (en) Method for providing oxidant with stable flow and purity for oxygen rich combustion supporting of kiln
CN111607672A (en) Oxygen enrichment process in front of blast furnace
CN102808053A (en) Oxygen-rich dry gas supply device for blast furnace iron-making
CN205917028U (en) Two medical molecular sieve oxygen generation systems of effect of single lobe pump
CN204918646U (en) Limekiln flue gas active ingredient retrieves and is used for converter mixed injection device
CN203731843U (en) Oxygen-rich nitrogen supply system for cupola furnace
CN103908869A (en) Vacuum pressure swing adsorption (VPSA) oxygen enrichment process
CN210814554U (en) System applied to oxygen-enriched combustion of coal-fired power plant boiler
CN107033978A (en) A kind of mine present low gas recycle device
CN204778820U (en) A device is prepared to oxygen boosting for natural gas burning
CN203591703U (en) Static gas mixing device and oxygen generation system for supporting combustion of rotary kiln
CN113028844A (en) Blast furnace hot blast stove flue gas waste heat recovery device and recovery method
CN202390202U (en) Device for supplying oxidant with stable flow and purity to oxygen-enriched combustion supporting of kiln

Legal Events

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

Granted publication date: 20130403