CN206112947U - 一种煤和生活垃圾耦合燃烧系统 - Google Patents
一种煤和生活垃圾耦合燃烧系统 Download PDFInfo
- Publication number
- CN206112947U CN206112947U CN201621103694.2U CN201621103694U CN206112947U CN 206112947 U CN206112947 U CN 206112947U CN 201621103694 U CN201621103694 U CN 201621103694U CN 206112947 U CN206112947 U CN 206112947U
- Authority
- CN
- China
- Prior art keywords
- coal
- pulverized
- fired boiler
- blower fan
- mixing chamber
- Prior art date
Links
- 239000003245 coal Substances 0.000 title claims abstract description 75
- OKTJSMMVPCPJKN-UHFFFAOYSA-N carbon Chemical compound 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[C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 title claims abstract description 55
- 238000002485 combustion reactions Methods 0.000 title claims abstract description 17
- 230000001808 coupling Effects 0.000 title claims abstract description 14
- 238000010168 coupling process Methods 0.000 title claims abstract description 14
- 238000005859 coupling reactions Methods 0.000 title claims abstract description 14
- 239000010791 domestic waste Substances 0.000 title abstract description 7
- 239000007789 gases Substances 0.000 claims abstract description 15
- 238000002309 gasification Methods 0.000 claims description 22
- 238000002156 mixing Methods 0.000 claims description 19
- 239000003570 air Substances 0.000 claims description 18
- 230000015572 biosynthetic process Effects 0.000 claims description 10
- 239000000779 smoke Substances 0.000 claims description 10
- 238000003786 synthesis reactions Methods 0.000 claims description 10
- 230000002194 synthesizing Effects 0.000 claims description 10
- UGFAIRIUMAVXCW-UHFFFAOYSA-N carbon monoxide Chemical compound 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Classifications
-
- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E20/00—Combustion technologies with mitigation potential
- Y02E20/12—Heat utilisation in combustion or incineration of waste
Abstract
Description
技术领域
[0001] 本实用新型涉及燃煤发电技术领域,尤其涉及一种煤和生活垃圾耦合燃烧系统。 背景技术
[0002] 我国城市生活垃圾总量大,并保持着较高的增速。根据国家统计局的数据,2014年全国生活垃圾清运量已达到1.786亿吨。城市生活垃圾成分复杂,含多种有毒、有害、难降解的成分,如果不对城市生活垃圾加以有效的处理和处置,会严重污染环境,影响人们的身体健康。因此,城市生活垃圾的处理和资源化利用,已成为环境保护的重点领域之一。
[0003] 针对城市生活垃圾的减量化、无害化和资源化需求,有破碎、压实、分选等预处理技术,和填埋、堆肥、厌氧发酵、焚烧和热解等处置技术。2014年末,我国生活垃圾卫生填埋无害化处理厂604座,生活垃圾卫生填埋无害化处理量10744.3万吨;生活垃圾焚烧无害化处理厂188座,生活垃圾焚烧无害化处理量5329.9万吨。可见,在我国填埋和焚烧是两种最主要的生活垃圾处置技术,且现阶段填埋的比例还显著高于焚烧。
[0004] 生活垃圾填埋的应用历史悠久,技术成熟,但减量的程度低,占用土地面积大,填埋场选址日益困难。焚烧技术的优点是减容、减量程度高,无害化彻底,可以回收利用垃圾中蕴含的热能,用于生产蒸汽和发电,实现资源化利用。因此,生活垃圾焚烧技术在国内的应用日益增多。
[0005] 目前,生活垃圾焚烧的主流设备是炉排炉和流化床焚烧炉两种。这两种设备可以适应生活垃圾热值低、成分复杂的特点,但炉内焚烧温度相比于电站煤粉锅炉等燃烧装置要低许多,所生产蒸汽的参数和发电效率也相对较低。
[0006] 我国有大量的电站煤粉锅炉。发展依托电站煤粉锅炉的煤和生活垃圾耦合发电技术,充分发挥大容量高参数火力发电厂燃烧温度高、污染物去除率高、发电效率高的技术优势,对于促进生活垃圾资源化利用和环境保护有积极意义。实用新型内容
[0007] 基于此,针对上述技术问题,提供一种煤和生活垃圾耦合燃烧系统。
[0008] 为解决上述技术问题,本实用新型采用如下技术方案:
[0009] —种煤和生活垃圾耦合燃烧系统,包括磨煤机、垃圾贮坑、给料器、气化炉以及合成气增压风机,所述磨煤机的出料口与煤粉锅炉的燃烧器连接,所述垃圾贮坑经所述给料器与所述气化炉的进料口连接,所述气化炉的出料口经所述合成气增压风机与所述煤粉锅炉的燃烧器连接。
[0010] 本方案还包括除尘器、冷烟风机以及混合室,所述除尘器设于所述煤粉锅炉的烟道尾部,其出口经所述冷烟风机与混合室的冷烟进口连接,所述混合室的热烟进口与所述煤粉锅炉的高温炉烟抽取口连接,且该混合室的混合烟气出口与所述气化炉的气化剂入口连接。
[0011] 本方案还包括空气预热器、第一风机以及第二风机,所述空气预热器设于所述煤粉锅炉的烟道尾部,其空气进口与所述第一风机以及第二风机连接,且其一次风出口与所述磨煤机连接,二次风出口与所述煤粉锅炉的燃烧器连接。
[0012] 所述二次风出口还与所述混合室连接。
[0013] 所述给料器内具有脱氯添加剂。
[0014] 本方案还包括煤斗以及给煤机,所述煤斗与给煤机连接,所述给煤机与所述磨煤机连接。
[0015] 本实用新型系统实现了燃煤发电、污泥干化和燃烧的有机结合,具有处理量大、流程简洁、气密性好的优势,其具有如下优点:
[0016] (1)风扇磨直吹式污泥干化制粉系统和常规煤粉制备系统组合使用,适用于高含水率污泥和煤的耦合燃烧发电。
[0017] (2)该系统中同时完成污泥干化和制粉,不需要进行干化污泥的长距离转运,流程短,设备少;垃圾贮坑至风扇磨入口均为负压系统,风扇磨出口至煤粉锅炉燃烧器之间的连接管路为气密性好的钢制承压管道,可充分避免粉尘和污泥中逸出的臭气扩散到环境中。
[0018] (3)该系统中污泥干化制粉后直接送入炉膛,这种直吹式制粉系统避免了污泥粉末的分离和储存环节,相比于中储式污泥干化制粉系统,可减少设备和初投资,降低系统阻力,有效消除干化污泥分离和储存过程中挥发分析出、缓慢氧化和自燃的风险。
[0019] (4)该系统对高含水率污泥的干化制粉能力可达100t/h以上,有利于实现污泥的大规模处置。附图说明
[0020] 下面结合附图和具体实施方式本实用新型进行详细说明:
[0021] 图1为本实用新型的结构示意图。具体实施方式
[0022] 如图1所示,一种煤和生活垃圾耦合燃烧系统,包括煤斗1、给煤机2、磨煤机3、垃圾贮坑4、给料器5、气化炉6以及合成气增压风机7。
[0023] 煤斗1与给煤机2连接,给煤机2与磨煤机3连接。
[0024] 磨煤机3的出料口与煤粉锅炉14的燃烧器14a连接。
[0025] 垃圾贮坑4经给料器5与气化炉6的进料口连接,气化炉6的出料口经合成气增压风机7与煤粉锅炉14的燃烧器14a连接。
[0026] 煤斗1中的原煤经给煤机2送入磨煤机3,磨煤机3出料口的一次风粉混合物输送到煤粉锅炉14的燃烧器14a。
[0027] 垃圾贮坑4中的生活垃圾经给料器5输送到气化炉6,与送入气化炉6中的气化剂接触并发生气化反应,产生的合成气进入合成气增压风机7,然后送至煤粉锅炉燃烧器14中燃烧,气化灰渣经气化炉6下部排出后用于铺路、制砖等资源化利用。
[0028] 本系统实现了燃煤发电、生活垃圾热处置的有机结合,具有高效、环保的优势,其具有以下特点:
[0029] (1)合成气送到煤粉锅炉,可方便地布置气体燃料燃烧器进行燃烧,克服了生活垃圾直接送入煤粉炉燃烧的破碎、制粉难题,而且煤粉燃烧形成的高温环境,可以在合成气热值不高或热值波动的工况下使其稳定燃烧,比单独利用合成气燃烧发电更稳定。
[0030] (4)与炉排炉、流化床焚烧炉相比,煤粉锅炉炉内火焰温度一般可高达1400-1600 °C,可避免合成气燃烧过程中二噁英的生成。
[0031] (5)与单独焚烧生活垃圾发电的系统相比,煤和合成气在高参数锅炉内燃烧后产生蒸汽,利用汽轮发电机组发电,可以提高循环效率,降低发电煤耗,是生活垃圾的热量得到更好利用。
[0032] 较佳的,给料器5内具有脱氯添加剂,垃圾贮坑4中的生活垃圾输送到给料器5中, 与脱氯添加剂混合,然后再进入气化炉6,这样可以从垃圾中析出的氯,减少氯向合成气中转移,减轻锅炉内受热面的腐蚀。
[0033] 本实施例还具有除尘器8、冷烟风机9以及混合室10,除尘器8设于煤粉锅炉14的烟道14b的尾部,其出口经冷烟风机9与混合室10的冷烟进口连接,混合室10的热烟进口与煤粉锅炉10的高温炉烟抽取口 14c连接,且该混合室10的混合烟气出口与气化炉6的气化剂入口连接。
[0034] 来自高温炉烟抽取口 14c的高温炉烟作为气化剂送入混合室10中,来自冷烟风机9 的低温炉烟同样作为气化剂送入混合室1 〇中。[〇〇35] 本实施例还具有空气预热器11、第一风机12以及第二风机13,空气预热器11设于煤粉锅炉14的烟道14b的尾部,其空气进口与第一风机11以及第二风机12连接,且其一次风出口与磨煤机3连接,二次风出口与煤粉锅炉14的燃烧器14a连接。
[0036] 第一风机12从环境中吸入空气,经空气预热器11加热后送入磨煤机3,第二风机13 从环境中吸入空气,经空气预热器11加热后送入燃烧器14a。[〇〇37] 较佳的,上述二次风出口还与混合室10连接,第二风机13从环境中吸入空气,经空气预热器11加热后,一部分送入燃烧器14a,另一部分送入混合室10,这样以高温炉烟/低温炉烟/热风混合介质为气化剂,可以灵活调节气化剂流量、温度和含氧量,适应不同季节或不同地域垃圾成分与热值的波动,保证气化炉工作稳定,提高气化效率。[〇〇38] 但是,本技术领域中的普通技术人员应当认识到,以上的实施例仅是用来说明本实用新型,而并非用作为对本实用新型的限定,只要在本实用新型的实质精神范围内,对以上所述实施例的变化、变型都将落在本实用新型的权利要求书范围内。
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CN108167838A (zh) * | 2017-12-26 | 2018-06-15 | 哈尔滨锅炉厂有限责任公司 | 一种垃圾焚烧炉嵌入大型燃煤锅炉的新型耦合发电系统 |
CN108916884A (zh) * | 2018-05-22 | 2018-11-30 | 华中科技大学 | 一种煤粉掺混垃圾的增氧燃烧方法 |
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CN108167838A (zh) * | 2017-12-26 | 2018-06-15 | 哈尔滨锅炉厂有限责任公司 | 一种垃圾焚烧炉嵌入大型燃煤锅炉的新型耦合发电系统 |
CN108916884A (zh) * | 2018-05-22 | 2018-11-30 | 华中科技大学 | 一种煤粉掺混垃圾的增氧燃烧方法 |
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