CN103276139A - Nitrogen dilution anti-explosion system in dry-method cooling and purifying recovery system for converter gas - Google Patents

Nitrogen dilution anti-explosion system in dry-method cooling and purifying recovery system for converter gas Download PDF

Info

Publication number
CN103276139A
CN103276139A CN2013102290076A CN201310229007A CN103276139A CN 103276139 A CN103276139 A CN 103276139A CN 2013102290076 A CN2013102290076 A CN 2013102290076A CN 201310229007 A CN201310229007 A CN 201310229007A CN 103276139 A CN103276139 A CN 103276139A
Authority
CN
China
Prior art keywords
nitrogen
explosion
pneumatic
smoke
electrostatic precipitator
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.)
Granted
Application number
CN2013102290076A
Other languages
Chinese (zh)
Other versions
CN103276139B (en
Inventor
王永刚
李俊辉
李朝阳
郭启超
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.)
China National Heavy Machinery Research Institute Co Ltd
Original Assignee
China National Heavy Machinery Research Institute 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 China National Heavy Machinery Research Institute Co Ltd filed Critical China National Heavy Machinery Research Institute Co Ltd
Priority to CN201310229007.6A priority Critical patent/CN103276139B/en
Publication of CN103276139A publication Critical patent/CN103276139A/en
Application granted granted Critical
Publication of CN103276139B publication Critical patent/CN103276139B/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Classifications

    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P10/00Technologies related to metal processing
    • Y02P10/20Recycling

Abstract

The invention provides a nitrogen dilution anti-explosion system in a dry-method cooling and purifying recovery system for a converter gas. The nitrogen dilution anti-explosion system mainly comprises a nitrogen tank, a rapid pneumatic valve arranged on a nitrogen pipe, a gas analyzer mounted on a smoke inlet pipeline of an electrostatic precipitator, as well as a controller, wherein the controller is used for controlling the rapid pneumatic valve to open or close according to a signal collected by the gas analyzer. The nitrogen dilution anti-explosion system can be mounted on the pipeline before smoke entering the electrostatic precipitator, smoke components can be detected timely, when smoke is in an explosion limit range, nitrogen is instantly sprayed into a flue for dilution, and accordingly, the explosion in the electrostatic precipitator is reduced or prevented.

Description

A kind of converter gas dry method cooling purifies the nitrogen dilution explosion protection system in the recovery system
Technical field
The invention belongs to a kind of coal gas dilution explosion protection system device, it is adapted to the converter gas dry method cooling and purifies in the recovery system, also can be applied in the dilution of poisonous or explosion hazard gases of other industry, be specifically related to a kind of converter gas dry method cooling and purify nitrogen dilution explosion protection system in the recovery system.
Background technology
Purify recovery and utilize the coal gas of converter technology at first from Japan, this and Japan Energy lack much relations.Japan's beginning in 1962 has just been installed wet method (OG method) converter coal gas purification recovery system in Yawata steel mill, real worldwide build RECOVERY OF CONVERTER GAS equipment last century the mid-1970s energy dilemma begin.Originally developing wet method (OG method) is that it is to blast within it for fear of coal gas of converter that this method does not adopt high-pressure static cleaner because coal gas of converter is a kind of flammable explosive gas, and wet method (OG method) it give a kind of psychology of people the steady and sure sense of security.Yet the West Germany Shandong is strange, the first cover coal gas of converter high-pressure electrostatic precipitation purification recovery system has been installed in exploitation in 1969 and in the Pai Na of Sa Erjite steel mill by Thyssen Aktiengesellschaft, and it is exactly converter gas dry method (LT method) first complete equipment.
In recent years, China advocates energetically aspect energy-saving and emission-reduction and promotes converter gas dry method cooling purification recovery technology, it is than Wet technique not only energy-conservation but also environmental protection, but in order to reduce the venting of dust explosion of the electric precipitator in this system, this technology is had higher requirement to the flushing and casting of converter, opens oxygen blast where such as the oxygen rifle, open oxygen blown intensity for what etc., in order to reduce the constraint to flushing and casting, also for fear of the stokehold unforeseen circumstances.It is periodic that Converter Oxigen Blowing is smelted, and smoke components (mainly is CO, CO 2, N 2, O 2) also change with smelting cycle, electrostatic precipitator is the crucial dust removal installation in this system, there is the phenomenon of high pressure static electricity discharge generation electric arc electrostatic precipitator inside, therefore the periodically variable flue gas that enters probably within it portion blast, therefore need the smoke components that enter in the electrostatic precipitator be detected and control, prevent the generation of exploding.And still there is not this antiknock device at present.
Summary of the invention
The purpose of this invention is to provide the nitrogen dilution explosion protection system in a kind of converter gas dry method cooling purification recovery system, so that the smoke components that enters in the electrostatic precipitator is detected and controls, prevent the generation of exploding.
For this reason, the invention provides the cooling of a kind of converter gas dry method and purify nitrogen dilution explosion protection system in the recovery system, mainly by nitrogen pot, be arranged on pneumatic immediate action valve on the nitrogen pipeline, be installed in the gas analyzer on the smoke-intake pipe road of electrostatic precipitator and control the controller that pneumatic immediate action valve opens or close according to the acquired signal of this gas analyzer and constitute.
Above-mentioned nitrogen pipeline is provided with the ball valve that places between pneumatic immediate action valve and the nitrogen pot.
Above-mentioned nitrogen pipeline is provided with reverse checkvalve, and this reverse checkvalve places pneumatic outlet one side of pneumatic immediate action valve.
Nitrogen dilution explosion protection system provided by the invention can be installed in flue gas and enter on the preceding pipeline of electrostatic precipitator, can detect smoke components in good time, moment sprays into nitrogen in the flue and dilutes in the time of in flue gas is in the limits of explosion scope, thereby reduces or avoid blasting in the electric precipitator.
Description of drawings
Below with reference to accompanying drawing the present invention is described in further details:
Fig. 1 is the application synoptic diagram that a kind of converter gas dry method cooling purifies the nitrogen dilution explosion protection system in the recovery system.
Among the figure: 1, nitrogen pot; 2, pneumatic immediate action valve; 3, gas analyzer; 4, nitrogen pipeline; 5, ball valve; 6, reverse checkvalve; 7, electrostatic precipitator; 8, smoke-intake pipe road.
Embodiment
In order to realize that the smoke components that enters in the electrostatic precipitator is detected and controls, prevent the generation of exploding, present embodiment provides a kind of converter gas dry method shown in Figure 1 cooling to purify nitrogen dilution explosion protection system in the recovery system, mainly by nitrogen pot 1, be arranged on pneumatic immediate action valve 2 on the nitrogen pipeline 4, be installed in the gas analyzer 3 on the smoke-intake pipe road of electrostatic precipitator and control the controller that pneumatic immediate action valve 2 opens or close according to the acquired signal of this gas analyzer 3 and constitute.Can detect smoke components by the gas analyzer 3 that is installed on the smoke-intake pipe road 8 before flue gas enters electrostatic precipitator 7 in good time, in the time of in flue gas is in the limits of explosion scope, open pneumatic immediate action valve 2 on the nitrogen pipeline 4 by controller (Controlling System), moment sprays into nitrogen in the flue and dilutes, thereby reduces or avoid blasting in the electric precipitator.
For the ease of maintenance and maintenance, present embodiment nitrogen pipeline 4 is provided with the ball valve 5 that places between pneumatic immediate action valve 2 and the nitrogen pot 1.And in order to prevent that coal gas from pouring in down a chimney in the nitrogen pipeline 4, be provided with reverse checkvalve 6 in the nitrogen pipeline 4 of pneumatic outlet one side of pneumatic immediate action valve 2.
In sum, be not difficult to find out that converter gas dry method cooling that present embodiment provides purifies the venting of dust explosion frequency that nitrogen dilution explosion protection system in the recovery system has not only reduced electric precipitator, guaranteed safety in production, and guaranteed the operating rate of converter, energy-conserving and environment-protective, non-secondary pollution again, and running cost is low.It should be noted that the nitrogen pressure that feeds in the present embodiment is generally 0.8MPa, flow is 2000~3500 Nm 3/ h, nitrogen gas purity is not less than 99.99%.
More than exemplifying only is to illustrate of the present invention, does not constitute the restriction to protection scope of the present invention, and the every and same or analogous design of the present invention all belongs within protection scope of the present invention.
The parts that present embodiment is not described in detail and structure belong to well-known components and common structure or the conventional means of the industry, here not narration one by one.

Claims (3)

1. converter gas dry method cooling purifies the nitrogen dilution explosion protection system in the recovery system, it is characterized in that: mainly by nitrogen pot (1), be arranged on pneumatic immediate action valve (2) on the nitrogen pipeline (4), be installed in the gas analyzer (3) on the smoke-intake pipe road (8) of electrostatic precipitator (7) and control the controller that pneumatic immediate action valve (2) opens or close according to the acquired signal of this gas analyzer (3) and constitute.
2. nitrogen dilution explosion protection system as claimed in claim 1, it is characterized in that: described nitrogen pipeline (4) is provided with the ball valve (5) that places between pneumatic immediate action valve (2) and the nitrogen pot (1).
3. nitrogen dilution explosion protection system as claimed in claim 1 or 2, it is characterized in that: described nitrogen pipeline (4) is provided with reverse checkvalve (6), and this reverse checkvalve (6) places pneumatic outlet one side of pneumatic immediate action valve (2).
CN201310229007.6A 2013-06-09 2013-06-09 Nitrogen dilution explosion protection system in a kind of converter gas dry method cooling, purifying recovery system Active CN103276139B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201310229007.6A CN103276139B (en) 2013-06-09 2013-06-09 Nitrogen dilution explosion protection system in a kind of converter gas dry method cooling, purifying recovery system

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201310229007.6A CN103276139B (en) 2013-06-09 2013-06-09 Nitrogen dilution explosion protection system in a kind of converter gas dry method cooling, purifying recovery system

Publications (2)

Publication Number Publication Date
CN103276139A true CN103276139A (en) 2013-09-04
CN103276139B CN103276139B (en) 2015-09-16

Family

ID=49058754

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201310229007.6A Active CN103276139B (en) 2013-06-09 2013-06-09 Nitrogen dilution explosion protection system in a kind of converter gas dry method cooling, purifying recovery system

Country Status (1)

Country Link
CN (1) CN103276139B (en)

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104084701A (en) * 2014-06-20 2014-10-08 张婧如 Device for recovering nitrogen during laser cutting of wood
CN106048131A (en) * 2016-08-05 2016-10-26 中冶赛迪工程技术股份有限公司 Converter electric precipitator system-based explosion-proof control method and device
CN107421580A (en) * 2017-05-27 2017-12-01 山西大学 A kind of dual field air-locked type electric cleaner test device
CN108265154A (en) * 2018-03-04 2018-07-10 北京首钢国际工程技术有限公司 A kind of automatic control system for preventing converter smelting coal gas venting of dust explosion
CN108265152A (en) * 2016-12-30 2018-07-10 北京凯德恒源科技发展有限公司 Pneumatic steelmaking coal gas complete recovering technique and its control method based on nitrogen compensation
CN108591826A (en) * 2018-04-23 2018-09-28 睿力集成电路有限公司 Gas handling system and processing method
CN111992009A (en) * 2020-08-26 2020-11-27 安徽华创环保设备科技有限公司 Tail gas purification early warning system based on regeneration metal smelting

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101554617A (en) * 2008-12-17 2009-10-14 中国重型机械研究院 Method for designing cylindrical horizontal wet electrical dust precipitator
CN101570808A (en) * 2009-05-31 2009-11-04 中冶京诚工程技术有限公司 Dry converter coal gas dust-removal system and explosion protection device thereof
CN201411467Y (en) * 2009-05-31 2010-02-24 中冶京诚工程技术有限公司 Dry dust removal system of converter gas and anti-explosion device thereof
CN101875993A (en) * 2010-07-30 2010-11-03 中冶南方工程技术有限公司 System for removing dust from converter gas by dry method and using method thereof

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101554617A (en) * 2008-12-17 2009-10-14 中国重型机械研究院 Method for designing cylindrical horizontal wet electrical dust precipitator
CN101570808A (en) * 2009-05-31 2009-11-04 中冶京诚工程技术有限公司 Dry converter coal gas dust-removal system and explosion protection device thereof
CN201411467Y (en) * 2009-05-31 2010-02-24 中冶京诚工程技术有限公司 Dry dust removal system of converter gas and anti-explosion device thereof
CN101875993A (en) * 2010-07-30 2010-11-03 中冶南方工程技术有限公司 System for removing dust from converter gas by dry method and using method thereof

Cited By (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104084701A (en) * 2014-06-20 2014-10-08 张婧如 Device for recovering nitrogen during laser cutting of wood
CN104084701B (en) * 2014-06-20 2016-05-11 盐城雄鹰精密机械有限公司 Nitrogen gas recovering apparatus in timber laser cutting
CN106048131A (en) * 2016-08-05 2016-10-26 中冶赛迪工程技术股份有限公司 Converter electric precipitator system-based explosion-proof control method and device
CN106048131B (en) * 2016-08-05 2019-05-03 中冶赛迪工程技术股份有限公司 Explosion prevention controlling process and device based on converter electric precipitator system
CN108265152A (en) * 2016-12-30 2018-07-10 北京凯德恒源科技发展有限公司 Pneumatic steelmaking coal gas complete recovering technique and its control method based on nitrogen compensation
CN107421580A (en) * 2017-05-27 2017-12-01 山西大学 A kind of dual field air-locked type electric cleaner test device
CN107421580B (en) * 2017-05-27 2023-06-02 山西大学 Double-electric-field air locking type electric dust collector testing device
CN108265154A (en) * 2018-03-04 2018-07-10 北京首钢国际工程技术有限公司 A kind of automatic control system for preventing converter smelting coal gas venting of dust explosion
CN108591826A (en) * 2018-04-23 2018-09-28 睿力集成电路有限公司 Gas handling system and processing method
CN111992009A (en) * 2020-08-26 2020-11-27 安徽华创环保设备科技有限公司 Tail gas purification early warning system based on regeneration metal smelting
CN111992009B (en) * 2020-08-26 2022-05-17 安徽华创环保设备科技有限公司 Tail gas purification early warning system based on regeneration metal smelting

Also Published As

Publication number Publication date
CN103276139B (en) 2015-09-16

Similar Documents

Publication Publication Date Title
CN103276139B (en) Nitrogen dilution explosion protection system in a kind of converter gas dry method cooling, purifying recovery system
CN101736117B (en) Converter fume high-temperature bag dust removal and recycling and secondary steam recycling system
CN102878822B (en) Device and method for purifying and recycling furnace gas of hermetic ore smelting furnace
CN107998817B (en) Single tower type fume purifier flue gas purification method
CN103388047B (en) Converter dry dust-removal system and technique
CN204127984U (en) A kind of industrial smoke dedusting and waste-heat recovery device
CN104061794A (en) Sintering air bellow exhausting gas waste heat circulating utilization device and method
CN111575435B (en) Primary dry dedusting system and method for ultra-clean gas recovery converter
CN203291682U (en) Double-protection safety device for sintering flue gas desulfurization and denitrification through activated carbon
CN102060197A (en) Pneumatic conveying method and system of pulverized coal
CN204694091U (en) A kind of recovery system of electric furnace zinc smelting tail gas
CN101230279B (en) Vehicle mounted coke oven coke-pusher smoke trapping system
CN105603148B (en) Pure the dry-method bag-type dust collecting system and technique of steelmaking converter flue gas heat recovery
CN2790564Y (en) Plastic plate dust separator
CN103451356A (en) Coarse dust-removal device for dry dust removal for converter
CN211328914U (en) Composite catalytic desulfurization system
CN101457274B (en) Explosion suppression system and method applied to steel converter gas recovery
CN104949533B (en) A kind of recovery system of electric furnace zinc smelting tail gas and its control method
CN208712489U (en) The connection structure of cement kiln flue gas introducing CCUS system
CN202398250U (en) Integrated treatment system for tail gas of calcium carbide furnace
CN201740409U (en) Device recovering waste heat from tail gas of closed calcium carbide furnace
CN108265152B (en) Converter steelmaking gas full recovery process based on nitrogen compensation and control method thereof
CN106591534B (en) Semidry duster and technique of the steelmaking converter flue gas with waste heat recovery
CN103162548A (en) Calcium-spraying humidification activation flue gas purification system of double-chamber melting furnace for secondary aluminum
CN201817509U (en) Converter coal gas dry-method dedusting system

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination
C14 Grant of patent or utility model
GR01 Patent grant