CN103363519A - Blast cap of fluidized bed furnace - Google Patents

Blast cap of fluidized bed furnace Download PDF

Info

Publication number
CN103363519A
CN103363519A CN2013103359685A CN201310335968A CN103363519A CN 103363519 A CN103363519 A CN 103363519A CN 2013103359685 A CN2013103359685 A CN 2013103359685A CN 201310335968 A CN201310335968 A CN 201310335968A CN 103363519 A CN103363519 A CN 103363519A
Authority
CN
China
Prior art keywords
fluidized bed
blast cap
bed furnace
blast
hot
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.)
Pending
Application number
CN2013103359685A
Other languages
Chinese (zh)
Inventor
游光刚
吴子汉
徐春
李宇琴
石彪
朱胜
罗川湖
李洪开
刘江
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.)
Wengfu Group Co Ltd
Original Assignee
Wengfu Group 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 Wengfu Group Co Ltd filed Critical Wengfu Group Co Ltd
Priority to CN2013103359685A priority Critical patent/CN103363519A/en
Publication of CN103363519A publication Critical patent/CN103363519A/en
Pending legal-status Critical Current

Links

Images

Abstract

The invention provides a blast cap of a fluidized bed furnace. The blast cap is cylindric and provided with a blast cap hole. The blast cap is characterized in that the diameter of the blast cap hole is 6 to 7 mm. The blast cap of the fluidized bed furnace provided by the invention overcomes biases in the prior art and has the following effects and advantages: 1, the boiling effect of the fluidized bed furnace is obviously better; 2, furnace temperature is substantially increased; 3, a hot blast rate is greatly increased, and output and quality of hot blast are improved; 4, the operation rate of the fluidized bed furnace is enhanced through improvement of the blast cap; and 5, the environment is improved, and surge is eliminated. According to practical usage, the blast cap of the fluidized bed furnace enables a preset purpose to be achieved and is applicable to fluidized bed furnaces.

Description

A kind of hood of fluidized bed furnace
Technical field
The present invention relates to chemical production technical field, relate in particular to a kind of hood of fluidized bed furnace.
Background technology
The production of drop sulfur ammonium mainly is to adopt " the dry internal return integrated technique of slurry-spraying pelletizing ", must utilize hot-blast stove that enough hot blasts are provided.Hot-blast stove adopts the Boiling Combustion mode, and capital equipment comprises boil air heater main body, blast cap and attached upper coal facility.The flue gas that burning produces through the sedimentation dedusting after, allocate cold wind into and regulate and reach required temperature and send into spray granulation drier and carry out dry materials by mending air-valve.In process of production, boil air heater blast cap eye is often blocked by cinder and causes the blast cap eye to diminish, and causes air blast to diminish by the air quantity that the blast cap eye blasts, burner hearth fuel boiling deleterious, stove provides hot blast rate inadequate, has a strong impact on product quality and produces load.Also occurred very large problem on product quality: nitrogen content often not, granularity descends, and intensity descends, and the product moisture absorption, product surface is rough, the product aberration is larger etc.Be that through the crux that must go wrong after the investigation and analysis boil air heater blast cap eye major part is blocked.Want to deal with problems, must reprocess transformation to the blast cap eye.It has been generally acknowledged that the shape that change hood of fluidized bed furnace, such as Chinese patent ZL200720101514.1 " hood of fluidized bed furnace " and ZL201020290097.1 " a kind of hood of fluidized bed furnace ", all changed the shape of hood of fluidized bed furnace, but practical effect is unsatisfactory on boil air heater.
Summary of the invention
The object of the invention is to overcome the prejudice of prior art, practical, effective a kind of hood of fluidized bed furnace are provided, to improve fluidized bed furnace boiling effect, more hot blast rate is provided, thereby improves Yield and quality, improve environment.
To achieve these goals, technical scheme of the present invention is as follows: a kind of hood of fluidized bed furnace, be cylindric, and the blast cap eye is arranged on it, it is characterized in that described blast cap eye diameter is 6~7mm.
The present invention has overcome the prejudice of prior art, the effect of the invention and advantage:
1, hot-blast stove boiling successful improves,
2, fire box temperature obviously improves,
3, provide hot blast rate obviously to increase, Yield and quality improves.
4, pass through the operation ratio of blast cap improvement hot-blast stove.
5, improve environment, eliminate surge.
A kind of hood of fluidized bed furnace provided by the invention uses proof by reality, has reached predetermined purpose, is applicable to fluidized bed furnace.
Description of drawings
Accompanying drawing 1 is a kind of hood of fluidized bed furnace structural representation of the present invention;
Among the figure, 1 is the blast cap eye.
The specific embodiment
The invention will be further described below in conjunction with embodiment:
Embodiment:
The present invention uses at certain boil air heater, and the thermic load of boil air heater is 3350 * 10 4KJ/h, fire coal transports with dolly, and cinder is transported to outward specifies the stockyard.Through research and calculating, determine former blast cap is transformed, its blast cap eye (1) diameter is changed greatly, namely from before less than 5mm, change greatly 6~7mm, to increase its ventilation, enough hot blast rates are provided for postorder workshop section, thereby have improved output and product quality.
A kind of hood of fluidized bed furnace structure of the present invention as shown in Figure 1, a kind of hood of fluidized bed furnace is cylindric, and blast cap eye 1 is arranged on it, it is characterized in that described blast cap eye 1 diameter is 6~7mm.
Effect analysis:
Before not adopting the present invention, the coal breaker hammer is owing to long-term the use is worn, and broken coal effect ratio is with relatively poor, and the screen bar also is worn, and the gap broadens, and fire coal is thicker, boiling deleterious during burning; The air blast blow rate required is inadequate, can not blow burner hearth combustion slag; Air-heater exhausting amount is inadequate, and it is less to take hot blast rate away, and the fire box temperature accumulation raises, and the burner hearth fire coal turns white, easily coking, impact intensification control; Boil air heater combustion chamber blast cap eye is stopped up by cinder, and ventilation reduces, and air blast air blast effect is descended, and the boiling effect is bad, and fire box temperature be cannot get up.
By the investigation and analysis to original data record, can see that original product intensity is not high, the intensity average qualification rate only has about 78%, table specific as follows:
Month January February March April
Mean intensity: N 32.9 30.8 31.1 33.7
Qualification rate: % 86.4 73.9 71.4 82.9
Adopt the present invention May, to blast cap eye process and remould, air blast and air-heater facility are constant, and the present invention in June is used for boil air heater production, and the boiling successful improves, and fire box temperature obviously improves, and the stove resistance force diminishes provides hot blast rate obviously to increase.
Hearth of hot-blast stove temperature and hot blast temperature contrast:
Project Before the transformation After the transformation
The average inlet temperature of air-heater: ℃ 510 630
The average furnace bore temperature: ℃ 805 925
Product strength and the contrast of intensity qualification rate:
Month January February March April May June
Mean intensity: N 32.9 30.8 31.1 33.7 32.1 39.6
Qualification rate: % 86.4 73.9 71.4 82.9 79.2 100.0
? Before the transformation After the transformation
Mean intensity: N 32.1 39.6
Qualification rate: % 78.8 100.0
Average split run output 165 tons 186 tons
This shows that use proof by reality, the present invention has reached predetermined purpose.

Claims (1)

1. a hood of fluidized bed furnace is cylindric, and blast cap eye (1) is arranged on it, it is characterized in that described blast cap eye (1) diameter is 6~7mm.
CN2013103359685A 2013-08-05 2013-08-05 Blast cap of fluidized bed furnace Pending CN103363519A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN2013103359685A CN103363519A (en) 2013-08-05 2013-08-05 Blast cap of fluidized bed furnace

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN2013103359685A CN103363519A (en) 2013-08-05 2013-08-05 Blast cap of fluidized bed furnace

Publications (1)

Publication Number Publication Date
CN103363519A true CN103363519A (en) 2013-10-23

Family

ID=49365460

Family Applications (1)

Application Number Title Priority Date Filing Date
CN2013103359685A Pending CN103363519A (en) 2013-08-05 2013-08-05 Blast cap of fluidized bed furnace

Country Status (1)

Country Link
CN (1) CN103363519A (en)

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN86203652U (en) * 1986-06-12 1988-03-02 中船总公司第七○三研究所 Fluidizing reactor burning saw powder
CN2708992Y (en) * 2004-07-15 2005-07-13 云南驰宏锌锗股份有限公司 Economic environmental protection type fluidized kiln air distribution board
US20070200007A1 (en) * 2003-12-23 2007-08-30 Rob Stevens Spraying Device and Method for Fluidised Bed Granulation
CN203083351U (en) * 2013-02-18 2013-07-24 云南鸿泰博化工股份有限公司 Air distribution plate of fluidized bed furnace
CN203454117U (en) * 2013-08-05 2014-02-26 瓮福(集团)有限责任公司 Funnel cap of fluidized bed combustion boiler

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN86203652U (en) * 1986-06-12 1988-03-02 中船总公司第七○三研究所 Fluidizing reactor burning saw powder
US20070200007A1 (en) * 2003-12-23 2007-08-30 Rob Stevens Spraying Device and Method for Fluidised Bed Granulation
CN2708992Y (en) * 2004-07-15 2005-07-13 云南驰宏锌锗股份有限公司 Economic environmental protection type fluidized kiln air distribution board
CN203083351U (en) * 2013-02-18 2013-07-24 云南鸿泰博化工股份有限公司 Air distribution plate of fluidized bed furnace
CN203454117U (en) * 2013-08-05 2014-02-26 瓮福(集团)有限责任公司 Funnel cap of fluidized bed combustion boiler

Similar Documents

Publication Publication Date Title
CN100489393C (en) Blast-furnace coal powder injection method using waste gas of hot-blast stove flue as carrier
CN104131122B (en) A kind of iron-smelting process based on winding-up coal gas of high temperature
KR101304686B1 (en) Part reduced iron for blast furnace and method thereof
CN113372024B (en) Double-hearth kiln for calcining lime by using low-calorific-value fuel and calcining method
CN102605119A (en) Pulverized coal conveying and preheating device used in blast furnace pulverized coal blasting process
CN103122398A (en) Smoke self-circulation preheating coal dust injection technology and device
CN203373366U (en) Hot-blast stove system for achieving high blast temperature by only burning blast furnace
CN203454117U (en) Funnel cap of fluidized bed combustion boiler
CN103014205A (en) Method for supplying oxygen to blast furnace oxygen-enriched coal spray
CN106675601A (en) Dry quenching circulating gas and coke-oven flue gas waste heat coupling utilization method
CN103320561A (en) Hot-blast stove system for high air temperature by using pure blast furnace gas and method thereof
CN203718753U (en) Composite combustion device
CN103363519A (en) Blast cap of fluidized bed furnace
CN104487598B (en) Pulverized coal injection into blast furna and manufacture method thereof
CN102020997B (en) Repairing method for briquette collapse of tamping coke oven
CN218435886U (en) Device for producing pellet ore by using low-calorific-value fuel
CN104833210A (en) Sintering ignition furnace with function of waste heat recovery
CN103993110A (en) Novel pre-injection pre-heating process for blast furnace pulverized coal injection
CN101760212A (en) Cooling structure for dry method coke quenching
CN202576449U (en) Coal dust conveying and preheating process apparatus in coal injection process of blast furnace
CN103913056B (en) Alloy baking method
Chevychelov et al. Charging coke nuts in the batch bunker
CN104060006B (en) The method of winding-up material and application and blast-furnace smelting
CN203904371U (en) Novel multi-level sectional type preheater for blast furnace jetted pulverized coal
CN108396086A (en) A kind of method of blast furnace process large scale blowing bituminous coal

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination
C02 Deemed withdrawal of patent application after publication (patent law 2001)
WD01 Invention patent application deemed withdrawn after publication

Application publication date: 20131023