CN204694025U - 一种生物质导热油炉尾气利用处理装置 - Google Patents
一种生物质导热油炉尾气利用处理装置 Download PDFInfo
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- CN204694025U CN204694025U CN201520401703.5U CN201520401703U CN204694025U CN 204694025 U CN204694025 U CN 204694025U CN 201520401703 U CN201520401703 U CN 201520401703U CN 204694025 U CN204694025 U CN 204694025U
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- 239000002028 Biomass Substances 0.000 title claims abstract description 13
- 239000002912 waste gas Substances 0.000 title claims abstract description 12
- 239000002918 waste heat Substances 0.000 claims abstract description 21
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- 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
- Y02E20/30—Technologies for a more efficient combustion or heat usage
-
- 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
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P70/00—Climate change mitigation technologies in the production process for final industrial or consumer products
- Y02P70/10—Greenhouse gas [GHG] capture, material saving, heat recovery or other energy efficient measures, e.g. motor control, characterised by manufacturing processes, e.g. for rolling metal or metal working
Abstract
本实用新型公开了一种生物质导热油炉尾气利用处理装置，包括导热油锅炉、散热器、余热回收装置和热交换区，所述散热器为片式散热器，散热器的下方设有风扇，风扇为轴流式风扇，散热器的左右两侧通过管道分别与导热油锅炉和排烟管道连通，散热器的上方通过密闭的通气管道连接有导热油换热器；所述余热回收装置内设有热交换区与排气管，热交换区的右侧壁上设有冷水进水口，热交换区的左侧壁上设有热水出口，热交换区的上端设有上空腔。本实用新型经过导热油换热器换热后的热气流温度恰好满足秸秆类易燃物质的干燥要求，节省了能源；设置的二级余热回收装置能够对锅炉的余热进行回收利用，提高能量利用率。
Description
技术领域
[0001] 本实用新型涉及机械领域，具体是一种生物质导热油炉尾气利用处理装置。
背景技术
[0002]当前，生物质导热油炉的燃烧用放入燃料为生物质，如稻壳、麦糠、药渣、玉米芯、植物秸杆传热介质为导热油。能够利用废弃的生物质进行发热，供给整个厂区使用，导热油炉在使用过程中所产生的烟气中含有大量的颗粒物、粉尘以及热量，直接排出会对大气产生很大的污染，而燃料燃烧所产生的能量的利用率也十分低下。
实用新型内容
[0003] 本实用新型的目的在于提供一种结构简单、使用方便的生物质导热油炉尾气利用处理装置，以解决上述背景技术中提出的问题。
[0004] 为实现上述目的，本实用新型提供如下技术方案:
[0005] 一种生物质导热油炉尾气利用处理装置，包括导热油锅炉、散热器、余热回收装置和热交换区，所述散热器为片式散热器，散热器的下方设有风扇，风扇为轴流式风扇，散热器的左右两侧通过管道分别与导热油锅炉和排烟管道连通，散热器的上方通过密闭的通气管道连接有导热油换热器，导热油换热器通过密闭的余热利用管道连接有气流干燥机，余热利用管道外侧包裹有保温层；此外，所述散热器的中间设有与导热油换热器连通的气流通道，导热油换热器设有出油管，导热油锅炉设有余热进油口，导热油换热器通过出油管与导热油锅炉的余热进油口连通；所述余热回收装置内设有热交换区与排气管，热交换区的右侧壁上设有冷水进水口，热交换区的左侧壁上设有热水出口，热交换区的上端设有上空腔，上空腔通过竖直隔板分为左上空腔与右上空腔，左上空腔的左侧设有烟气进口，烟气进口连接排烟管道，右上空腔的上端设有烟气出口，烟气出口的上端连接灰尘处理装置，灰尘处理装置连接烟囱，此外，热交换区的下端设有下空腔，下空腔的前侧面上设有清灰口，热交换区的内部设有一个开口向上的竖直折流板，左上空腔与下空腔之间通过一组排气管连通，右上空腔与下空腔之间也通过一组排气管连通。
[0006] 进一步的:所述清灰口上设有密封盖。
[0007] 进一步的:所述两组排气管分别设在竖直折流板的两侧。
[0008] 进一步的:所述热水出口通过水管连接到热水供应管道。
[0009] 与现有技术相比，本实用新型的结构简单、使用方便，经过导热油换热器换热后的热气流温度恰好满足秸杆类易燃物质的干燥要求，节省了能源；设置的二级余热回收装置能够对锅炉的余热进行回收利用，提高能量利用率。
附图说明
[0010] 图1为一种生物质导热油炉尾气利用处理装置的结构示意图。
具体实施方式
[0011] 下面结合具体实施方式对本专利的技术方案作进一步详细地说明。
[0012] 请参阅图1，一种生物质导热油炉尾气利用处理装置，包括导热油锅炉1、散热器
2、余热回收装置26和热交换区27，所述散热器2为片式散热器，散热器2的下方设有风扇5，风扇5为轴流式风扇，散热器2的左右两侧通过管道分别与导热油锅炉I和排烟管道3连通，散热器2的上方通过密闭的通气管道7连接有导热油换热器8，导热油换热器8通过密闭的余热利用管道10连接有气流干燥机9，余热利用管道10外侧包裹有保温层，气流干燥机9和余热利用管道能够根据需要穿过相应的厂房；此外，所述散热器2的中间设有与导热油换热器8连通的气流通道，导热油换热器8设有出油管6，导热油锅炉I设有余热进油口 4，导热油换热器8通过出油管6与导热油锅炉I的余热进油口 4连通；使用时，导热油锅炉I开始加热，然后启动轴流式风扇5，向散热器2吹入空气，导热油锅炉I产生的热气流，热气流经过散热器2流向沉降罐14的过程中，散热器2内设有水平的气流通道，风扇5吹到导热油换热器8内部，经过热交换后的热空气沿余热利用管道10送至气流干燥机9，对气流干燥机9内的秸杆进行干燥，而导热油换热器8内的导热油吸收的热量经出油管6又重新送到导热油锅炉I内，作为热源供给，直接利用导热油锅炉I余热干燥秸杆的话，余热温度太高，会引燃秸杆，所以经过再次余热吸收，通过风扇的吹动，此时的余热温度刚好满足秸杆干燥的要求；所述余热回收装置26内设有热交换区27与排气管23，热交换区27的右侧壁上设有冷水进水口 21，热交换区27的左侧壁上设有热水出口 14，热水出口 14通过水管连接到热水供应管道，从而为人们日常生产和生活的用水提供方便，热交换区27的上端设有上空腔20，上空腔20通过竖直隔板19分为左上空腔与右上空腔，左上空腔的左侧设有烟气进口 15，烟气进口 15连接排烟管道3，右上空腔的上端设有烟气出口 18，烟气出口 18的上端连接灰尘处理装置17，灰尘处理装置17连接烟囱16，此外，热交换区27的下端设有下空腔24，下空腔24的前侧面上设有清灰口 25，清灰口 25上设有密封盖，通过清灰口 25能够对下空腔24内积累的烟尘进行清理，热交换区27的内部设有一个开口向上的竖直折流板27，左上空腔与下空腔24之间通过一组排气管23连通，右上空腔与下空腔24之间也通过一组排气管23连通，两组排气管23分别设在竖直折流板27的两侧；使用时，烟气从烟气进口 15进去左上空腔内，然后烟气通过左侧排气管23进去下空腔24内，然后烟气在下空腔24内转向并通过右侧的排气管23进入右上空腔内，冷水从冷水进口 26进入到热交换区27内，冷水在热交换区27内与排气管23内的烟气进行热交换，热交换后的冷水经过竖直折流板27从冷水出口 18流出；完成热交换后的烟气从右上空腔进入烟气出口 18内，其后，烟气再进入灰尘处理装置17内部进行除尘工作，经过处理的烟气最后从烟囱16排出。
[0013] 上面对本专利的较佳实施方式作了详细说明，但是本专利并不限于上述实施方式，在本领域的普通技术人员所具备的知识范围内，还可以在不脱离本专利宗旨的前提下作出各种变化。
Claims (4)
1.一种生物质导热油炉尾气利用处理装置，包括导热油锅炉(1)、散热器(2)、余热回收装置(26)和热交换区(27)，其特征在于，所述散热器(2)为片式散热器，散热器(2)的下方设有风扇(5)，风扇(5)为轴流式风扇，散热器(2)的左右两侧通过管道分别与导热油锅炉(I)和排烟管道(3)连通，散热器(2)的上方通过密闭的通气管道(7)连接有导热油换热器(8)，导热油换热器(8)通过密闭的余热利用管道(10)连接有气流干燥机(9)，余热利用管道(10)外侧包裹有保温层；此外，所述散热器(2)的中间设有与导热油换热器(8)连通的气流通道，导热油换热器(8)设有出油管(6)，导热油锅炉(I)设有余热进油口(4)，导热油换热器(8)通过出油管(6)与导热油锅炉(I)的余热进油口(4)连通；所述余热回收装置(26)内设有热交换区(27)与排气管(23)，热交换区(27)的右侧壁上设有冷水进水口(21)，热交换区(27)的左侧壁上设有热水出口(14)，热交换区(27)的上端设有上空腔(20)，上空腔(20)通过竖直隔板(19)分为左上空腔与右上空腔，左上空腔的左侧设有烟气进口(15)，烟气进口(15)连接排烟管道(3)，右上空腔的上端设有烟气出口(18)，烟气出口(18)的上端连接灰尘处理装置(17)，灰尘处理装置(17)连接烟囱(16)，此外，热交换区(27)的下端设有下空腔(24)，下空腔(24)的前侧面上设有清灰口(25)，热交换区(27)的内部设有一个开口向上的竖直折流板(27)，左上空腔与下空腔(24)之间通过一组排气管(23)连通，右上空腔与下空腔(24)之间也通过一组排气管(23)连通。
2.根据权利要求1所述的一种生物质导热油炉尾气利用处理装置，其特征在于，所述清灰口(25)上设有密封盖。
3.根据权利要求1所述的一种生物质导热油炉尾气利用处理装置，其特征在于，所述两组排气管(23)分别设在竖直折流板(27)的两侧。
4.根据权利要求1所述的一种生物质导热油炉尾气利用处理装置，其特征在于，所述热水出口(14)通过水管连接到热水供应管道。
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