CN111594850A - Grate type plasma gasification melting furnace - Google Patents
Grate type plasma gasification melting furnace Download PDFInfo
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- CN111594850A CN111594850A CN202010552781.0A CN202010552781A CN111594850A CN 111594850 A CN111594850 A CN 111594850A CN 202010552781 A CN202010552781 A CN 202010552781A CN 111594850 A CN111594850 A CN 111594850A
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- 238000002844 melting Methods 0.000 title claims abstract description 39
- 230000008018 melting Effects 0.000 title claims abstract description 39
- 238000009272 plasma gasification Methods 0.000 title claims abstract description 13
- 238000001035 drying Methods 0.000 claims abstract description 21
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 claims abstract description 11
- 239000003546 flue gas Substances 0.000 claims abstract description 11
- 239000000463 material Substances 0.000 claims description 9
- 239000005416 organic matter Substances 0.000 abstract description 9
- 238000006243 chemical reaction Methods 0.000 abstract description 6
- 238000000926 separation method Methods 0.000 abstract description 3
- 239000002910 solid waste Substances 0.000 description 9
- 239000002893 slag Substances 0.000 description 3
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 3
- 229910002091 carbon monoxide Inorganic materials 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 239000007789 gas Substances 0.000 description 2
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- 238000007254 oxidation reaction Methods 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- 230000009471 action Effects 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 239000004566 building material Substances 0.000 description 1
- 238000002485 combustion reaction Methods 0.000 description 1
- 238000005336 cracking Methods 0.000 description 1
- 230000004907 flux Effects 0.000 description 1
- 238000002309 gasification Methods 0.000 description 1
- 239000011521 glass Substances 0.000 description 1
- 229910001385 heavy metal Inorganic materials 0.000 description 1
- 239000007791 liquid phase Substances 0.000 description 1
- 239000003345 natural gas Substances 0.000 description 1
- 230000008569 process Effects 0.000 description 1
- 238000004886 process control Methods 0.000 description 1
- 238000006722 reduction reaction Methods 0.000 description 1
- 238000009270 solid waste treatment Methods 0.000 description 1
- 238000006467 substitution reaction Methods 0.000 description 1
- 239000002912 waste gas Substances 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
Images
Classifications
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G5/00—Incineration of waste; Incinerator constructions; Details, accessories or control therefor
- F23G5/02—Incineration of waste; Incinerator constructions; Details, accessories or control therefor with pretreatment
- F23G5/04—Incineration of waste; Incinerator constructions; Details, accessories or control therefor with pretreatment drying
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G5/00—Incineration of waste; Incinerator constructions; Details, accessories or control therefor
- F23G5/002—Incineration of waste; Incinerator constructions; Details, accessories or control therefor characterised by their grates
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G5/00—Incineration of waste; Incinerator constructions; Details, accessories or control therefor
- F23G5/02—Incineration of waste; Incinerator constructions; Details, accessories or control therefor with pretreatment
- F23G5/027—Incineration of waste; Incinerator constructions; Details, accessories or control therefor with pretreatment pyrolising or gasifying stage
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G5/00—Incineration of waste; Incinerator constructions; Details, accessories or control therefor
- F23G5/44—Details; Accessories
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G2203/00—Furnace arrangements
- F23G2203/101—Furnace arrangements with stepped or inclined grate
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- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Gasification And Melting Of Waste (AREA)
Abstract
本发明公开了一种炉排式等离子气化熔融炉,包括进料口,进料口上连接有预热干燥区,预热干燥区的出口连接有焚烧区,焚烧区的出口设有燃尽区,燃尽区的出口设有熔融区,熔融区上设有排出口,焚烧区的上方设有烟气出口。本发明中熔融炉实现了有机物反应与无机物熔融区域的分离,互不影响,调节简单,运行稳定,焚烧处理彻底。
The invention discloses a grate type plasma gasification melting furnace, which comprises a feeding port, a preheating and drying zone is connected to the feeding port, an incineration zone is connected to the outlet of the preheating and drying zone, and a burnout zone is arranged at the outlet of the incineration zone , the outlet of the burnout zone is provided with a melting zone, a discharge outlet is provided on the melting zone, and a flue gas outlet is provided above the incineration zone. In the present invention, the melting furnace realizes the separation of the organic matter reaction and the inorganic matter melting region, without mutual influence, simple adjustment, stable operation, and thorough incineration treatment.
Description
技术领域technical field
本发明属于熔融炉技术领域,具体涉及一种炉排式等离子气化熔融炉。The invention belongs to the technical field of melting furnaces, in particular to a grate type plasma gasification melting furnace.
背景技术Background technique
现有等离子气化熔融炉固废气化和熔融在一个炉体内,造成工艺控制难度大,炉排炉焚烧处理不彻底,残渣中还有未完全燃尽有机物。Existing plasma gasification melting furnaces solidify and melt waste gas in one furnace body, resulting in difficult process control, incomplete incineration treatment in the grate furnace, and incompletely burned organic matter in the residue.
发明内容SUMMARY OF THE INVENTION
本发明的目的在于提供一种炉排式等离子气化熔融炉,焚烧处理彻底。The purpose of the present invention is to provide a grate-type plasma gasification melting furnace with complete incineration treatment.
为实现上述目的,本发明提供如下技术方案:一种炉排式等离子气化熔融炉,包括进料口,所述进料口上连接有预热干燥区,所述预热干燥区的出口连接有焚烧区,所述焚烧区的出口设有燃尽区,所述燃尽区的出口设有熔融区,所述熔融区上设有排出口,所述焚烧区的上方设有烟气出口。In order to achieve the above purpose, the present invention provides the following technical solutions: a grate type plasma gasification melting furnace, comprising a feeding port, the feeding port is connected with a preheating and drying zone, and the outlet of the preheating and drying zone is connected with a Incineration zone, the outlet of the incineration zone is provided with a burnout zone, the outlet of the burnout zone is provided with a melting zone, a discharge port is provided on the melting zone, and a flue gas outlet is provided above the incineration zone.
进一步地,所述预热干燥区、焚烧区、燃尽区均通过机械炉排输送物料。Further, the preheating and drying zone, the incineration zone and the burnout zone all transport materials through a mechanical grate.
进一步地,所述预热干燥区的温度设置为500-600℃,所述焚烧区的温度设置为800-1000℃,所述燃尽区的温度设置为900-1100℃,所述熔融区1400-1600℃。Further, the temperature of the preheating and drying zone is set to 500-600°C, the temperature of the incineration zone is set to 800-1000°C, the temperature of the burnout zone is set to 900-1100°C, and the temperature of the melting zone is set to 1400°C. -1600℃.
进一步地,所述机械炉排采用逆推式炉排炉、顺推式炉排炉或往复翻动式炉排炉中的任意一种。Further, the mechanical grate adopts any one of a reverse push grate furnace, a forward push grate furnace or a reciprocating turning grate furnace.
进一步地,所述进料口的内壁铰接有两块相对设置的导料板,每个所述导料板的下方均设有连接气缸,所述连接气缸的外壳与进料口的内壁铰接,所述连接气缸的活塞杆与对应导料板铰接。Further, two oppositely arranged feed guide plates are hinged on the inner wall of the feed port, and a connecting cylinder is arranged below each of the feed guide plates, and the outer shell of the connecting cylinder is hinged with the inner wall of the feed port, The piston rod of the connecting cylinder is hinged with the corresponding material guide plate.
与现有技术相比,本发明的有益效果是。Compared with the prior art, the beneficial effects of the present invention are as follows.
(1)熔融炉实现了有机物反应与无机物熔融区域的分离,互不影响,调节简单,运行稳定,焚烧处理彻底。(1) The melting furnace realizes the separation of the organic matter reaction and the inorganic matter melting area, without affecting each other, with simple adjustment, stable operation, and thorough incineration treatment.
(2)固废在炉内停留时间可通过调节机械炉排运动结构实现。(2) The residence time of solid waste in the furnace can be realized by adjusting the motion structure of the mechanical grate.
附图说明Description of drawings
图1为本发明一种炉排式等离子气化熔融炉的结构示意图。FIG. 1 is a schematic structural diagram of a grate type plasma gasification melting furnace of the present invention.
图2为进料口的结构示意图。Figure 2 is a schematic structural diagram of the feed port.
图中:1、烟气出口;2、熔融区;3、燃尽区;4、焚烧区;5、预热干燥区;6、进料口;7、等离子炬;8、一次风;9、二次风;10、三次风;11、排渣口;12、连接气缸;13、导料板。In the figure: 1. Flue gas outlet; 2. Melting zone; 3. Burnout zone; 4. Incineration zone; 5. Preheating and drying zone; 6. Feed inlet; 7. Plasma torch; 8. Primary air; 9. Secondary air; 10. Tertiary air; 11. Slag discharge port; 12. Connecting cylinder; 13. Material guide plate.
具体实施方式Detailed ways
下面将结合本发明实施例中的附图,对本发明实施例中的技术方案进行清楚、完整地描述,显然,所描述的实施例仅仅是本发明一部分实施例,而不是全部的实施例。基于本发明中的实施例,本领域普通技术人员在没有做出创造性劳动前提下所获得的所有其他实施例,都属于本发明保护的范围。The technical solutions in the embodiments of the present invention will be clearly and completely described below with reference to the accompanying drawings in the embodiments of the present invention. Obviously, the described embodiments are only a part of the embodiments of the present invention, but not all of the embodiments. Based on the embodiments of the present invention, all other embodiments obtained by those of ordinary skill in the art without creative efforts shall fall within the protection scope of the present invention.
实施例一。Example 1.
请参阅图1-图2,本发明提供一种炉排式等离子气化熔融炉,包括进料口6,进料口6上连接有预热干燥区5,预热干燥区5的出口连接有焚烧区4,焚烧区4的出口设有燃尽区3,燃尽区3的出口设有熔融区2,熔融区2上设有排出口,焚烧区4的上方设有烟气出口1;预热干燥区5、焚烧区4、燃尽区3均通过机械炉排输送物料。Please refer to FIG. 1 to FIG. 2 , the present invention provides a grate type plasma gasification melting furnace, comprising a
预热干燥区5的温度设置为500-600℃,焚烧区4的温度设置为800-1000℃,燃尽区3的温度设置为900-1100℃,熔融区21400-1600℃,区域温度也需要根据处理固废特性不同进行调整;预热干燥区5、焚烧区4、燃尽区3可采用等离子炬7、天然气燃烧器、柴油燃烧器作为助燃系统,熔融区2可采用等离子炬7、助熔电极、浸没式燃烧器作为热源提供。The temperature of the preheating
熔融炉配风分成一次风8、二次风9、三次风10;一次风8包括预热干燥区5、焚烧区4、燃尽区3三个位置,根据区域温度调整配风量;二次风9通过等离子炬7进入,再次将燃尽区3残留的有机物分解;三次风10根据出口烟气中CO、H2、CH4、O2的含量进行调整;焚烧区4固废有机物采用气化反应还是氧化反应可通过调节一次风8实现。The air distribution of the melting furnace is divided into primary air 8,
机械炉排可采用逆推式炉排炉、顺推式炉排炉或往复翻动式炉排炉中的任意一种,根据固废水分、灰分、热值等特性选择。The mechanical grate can be any one of the reverse push grate furnace, the forward push grate furnace or the reciprocating turning grate furnace, and it is selected according to the characteristics of solid waste water content, ash content and calorific value.
固废通过进料口6进入预热干燥区5的机械炉排,在此区域500-600℃温度下,固废中水分全部蒸发,轻组分有机物裂解,此时固废体积缩小;再通过机械炉排移动到焚烧区4的机械炉排,在此区域800-1000℃温度下,通过调节一次风8,确保固废中有机物充分反应,在此过程即有氧化反应也有还原反应;再通过机械炉排移动到燃尽区3的机械炉排,在此区域温度比焚烧区4域温度高100℃以上,确保难分解有机物的充分裂解反应,此时固废中有机物基本反应彻底;剩余固废中无机物和重金属进入熔融区2,在熔融区2设置有等离子炬7和助熔电极,在两者能量输入下,确保熔融区2温度达到1400-1600℃,在此温度下,固废中无机物全部熔融变成液相,最后通过排渣口11排出,排出熔渣可通过水冷或者风冷得到玻璃体或者其他建筑材料;在炉内反应过程产生的气体通过出口负压作用下,向烟气出口1移动,在烟气出口1上部区域设置有三次风10,通过三次风10调节出口烟气中CO、H2、CH4、O2等气体成分,符合要求烟气通过烟气出口1排出炉内;在炉内不同区域设置不同的燃烧器,在预热干燥区5、焚烧区4、燃尽区3设置有燃烧器、等离子炬7提供能量,满足区域温度要求;熔融炉实现了有机物反应与无机物熔融区2域的分离,互不影响,调节简单,运行稳定。The solid waste enters the mechanical grate of the preheating and
实施例二。Example two.
本实施例与实施例一的区别在于,进料口6的内壁铰接有两块相对设置的导料板13,每个导料板13的下方均设有连接气缸12,连接气缸12的外壳与进料口6的内壁铰接,连接气缸12的活塞杆与对应导料板13铰接,当物料通过倒入进料口6中时,连接气缸12的活塞杆收缩,导料板13向下转动,将进料口6打开,物料进入到进料口6内,进料完成后活塞杆伸出,导料板13将进料口6关闭,减少了热量从进料口6损失;另外连接气缸12能够带动导料板13来回转动,避免了进料口6物料的堵塞。The difference between this embodiment and the first embodiment is that the inner wall of the
预热干燥区、焚烧区、燃尽区均通过机械炉排输送物料,预热干燥区的温度设置为550-600℃,焚烧区的温度设置为850-950℃,燃尽区的温度设置为920-1100℃,熔融区1450-1580℃,机械炉排可采用逆推式炉排炉、顺推式炉排炉或往复翻动式炉排炉中的任意一种。The preheating drying area, the incineration area and the burnout area are all conveyed by the mechanical grate. The temperature of the preheating drying area is set to 550-600℃, the temperature of the incineration area is set to 850-950℃, and the temperature of the burnout area is set to 920-1100 ℃, melting zone 1450-1580 ℃, mechanical grate can use any one of reverse push grate furnace, forward push grate furnace or reciprocating turning grate furnace.
尽管已经示出和描述了本发明的实施例,对于本领域的普通技术人员而言,可以理解在不脱离本发明的原理和精神的情况下可以对这些实施例进行多种变化、修改、替换和变型,本发明的范围由所附权利要求及其等同物限定。Although embodiments of the present invention have been shown and described, it will be understood by those skilled in the art that various changes, modifications, and substitutions can be made in these embodiments without departing from the principle and spirit of the invention and modifications, the scope of the invention is defined by the appended claims and their equivalents.
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