CN107520235A - 一种医疗废弃物的无碳排放处理方法 - Google Patents
一种医疗废弃物的无碳排放处理方法 Download PDFInfo
- Publication number
- CN107520235A CN107520235A CN201710771797.9A CN201710771797A CN107520235A CN 107520235 A CN107520235 A CN 107520235A CN 201710771797 A CN201710771797 A CN 201710771797A CN 107520235 A CN107520235 A CN 107520235A
- Authority
- CN
- China
- Prior art keywords
- waste
- carbon
- biohazard waste
- processing method
- reacting furnace
- 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.)
- Withdrawn
Links
- 239000002699 waste material Substances 0.000 title claims abstract description 43
- 238000003672 processing method Methods 0.000 title claims abstract description 16
- 239000007789 gas Substances 0.000 claims abstract description 21
- 239000007788 liquid Substances 0.000 claims abstract description 21
- 239000007787 solid Substances 0.000 claims abstract description 14
- 239000003054 catalyst Substances 0.000 claims abstract description 9
- 229920002521 macromolecule Polymers 0.000 claims abstract description 8
- 239000002906 medical waste Substances 0.000 claims abstract description 8
- 239000000047 product Substances 0.000 claims description 20
- 239000012265 solid product Substances 0.000 claims description 9
- 239000000126 substance Substances 0.000 claims description 5
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 4
- WSFSSNUMVMOOMR-UHFFFAOYSA-N Formaldehyde Chemical compound O=C WSFSSNUMVMOOMR-UHFFFAOYSA-N 0.000 claims description 4
- KFSLWBXXFJQRDL-UHFFFAOYSA-N Peracetic acid Chemical compound CC(=O)OO KFSLWBXXFJQRDL-UHFFFAOYSA-N 0.000 claims description 4
- 229910052799 carbon Inorganic materials 0.000 claims description 4
- 239000003814 drug Substances 0.000 claims description 3
- 239000000463 material Substances 0.000 claims description 3
- 238000010521 absorption reaction Methods 0.000 claims description 2
- 230000006835 compression Effects 0.000 claims description 2
- 238000007906 compression Methods 0.000 claims description 2
- 238000000354 decomposition reaction Methods 0.000 claims description 2
- 239000000645 desinfectant Substances 0.000 claims description 2
- 229940079593 drug Drugs 0.000 claims description 2
- 239000010781 infectious medical waste Substances 0.000 claims description 2
- 230000001678 irradiating effect Effects 0.000 claims description 2
- 239000010825 pathological waste Substances 0.000 claims description 2
- 230000005855 radiation Effects 0.000 claims description 2
- 210000002966 serum Anatomy 0.000 claims description 2
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 claims 2
- 239000003345 natural gas Substances 0.000 claims 1
- 238000000034 method Methods 0.000 abstract description 11
- 238000006243 chemical reaction Methods 0.000 abstract description 6
- 239000005416 organic matter Substances 0.000 abstract description 4
- 238000000197 pyrolysis Methods 0.000 abstract description 4
- 239000000295 fuel oil Substances 0.000 abstract description 3
- 238000010504 bond cleavage reaction Methods 0.000 abstract description 2
- 239000011203 carbon fibre reinforced carbon Substances 0.000 abstract description 2
- 230000008569 process Effects 0.000 abstract description 2
- 238000011084 recovery Methods 0.000 abstract description 2
- 230000007017 scission Effects 0.000 abstract description 2
- 239000011358 absorbing material Substances 0.000 abstract 1
- 238000005516 engineering process Methods 0.000 description 6
- 238000004458 analytical method Methods 0.000 description 4
- 238000004227 thermal cracking Methods 0.000 description 4
- 239000003921 oil Substances 0.000 description 3
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 3
- RAHZWNYVWXNFOC-UHFFFAOYSA-N Sulphur dioxide Chemical compound O=S=O RAHZWNYVWXNFOC-UHFFFAOYSA-N 0.000 description 2
- 238000005336 cracking Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 230000005611 electricity Effects 0.000 description 2
- 230000007613 environmental effect Effects 0.000 description 2
- 239000000446 fuel Substances 0.000 description 2
- 238000010438 heat treatment Methods 0.000 description 2
- 239000004615 ingredient Substances 0.000 description 2
- 238000004895 liquid chromatography mass spectrometry Methods 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 239000010813 municipal solid waste Substances 0.000 description 2
- 239000010453 quartz Substances 0.000 description 2
- 230000035484 reaction time Effects 0.000 description 2
- 230000009467 reduction Effects 0.000 description 2
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N silicon dioxide Inorganic materials O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 2
- 238000001228 spectrum Methods 0.000 description 2
- 230000001954 sterilising effect Effects 0.000 description 2
- 230000001988 toxicity Effects 0.000 description 2
- 231100000419 toxicity Toxicity 0.000 description 2
- 206010001488 Aggression Diseases 0.000 description 1
- 206010002660 Anoxia Diseases 0.000 description 1
- 241000976983 Anoxia Species 0.000 description 1
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 1
- 206010021143 Hypoxia Diseases 0.000 description 1
- ISWSIDIOOBJBQZ-UHFFFAOYSA-N Phenol Chemical compound OC1=CC=CC=C1 ISWSIDIOOBJBQZ-UHFFFAOYSA-N 0.000 description 1
- 230000004913 activation Effects 0.000 description 1
- 239000003463 adsorbent Substances 0.000 description 1
- 238000003915 air pollution Methods 0.000 description 1
- 230000007953 anoxia Effects 0.000 description 1
- 150000001491 aromatic compounds Chemical class 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- -1 carbohydrate organic compounds Chemical class 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 239000003245 coal Substances 0.000 description 1
- 238000002485 combustion reaction Methods 0.000 description 1
- 230000000052 comparative effect Effects 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 238000011038 discontinuous diafiltration by volume reduction Methods 0.000 description 1
- 238000004821 distillation Methods 0.000 description 1
- 238000002474 experimental method Methods 0.000 description 1
- 239000002737 fuel gas Substances 0.000 description 1
- 239000003502 gasoline Substances 0.000 description 1
- 239000004519 grease Substances 0.000 description 1
- 239000005431 greenhouse gas Substances 0.000 description 1
- IXCSERBJSXMMFS-UHFFFAOYSA-N hydrogen chloride Substances Cl.Cl IXCSERBJSXMMFS-UHFFFAOYSA-N 0.000 description 1
- 229910000041 hydrogen chloride Inorganic materials 0.000 description 1
- 239000002075 main ingredient Substances 0.000 description 1
- QSHDDOUJBYECFT-UHFFFAOYSA-N mercury Chemical compound [Hg] QSHDDOUJBYECFT-UHFFFAOYSA-N 0.000 description 1
- 229910052753 mercury Inorganic materials 0.000 description 1
- WSFSSNUMVMOOMR-NJFSPNSNSA-N methanone Chemical compound O=[14CH2] WSFSSNUMVMOOMR-NJFSPNSNSA-N 0.000 description 1
- 230000001575 pathological effect Effects 0.000 description 1
- 230000000505 pernicious effect Effects 0.000 description 1
- 150000003071 polychlorinated biphenyls Chemical class 0.000 description 1
- 238000004659 sterilization and disinfection Methods 0.000 description 1
- 238000005303 weighing Methods 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B09—DISPOSAL OF SOLID WASTE; RECLAMATION OF CONTAMINATED SOIL
- B09B—DISPOSAL OF SOLID WASTE NOT OTHERWISE PROVIDED FOR
- B09B3/00—Destroying solid waste or transforming solid waste into something useful or harmless
- B09B3/0075—Disposal of medical waste
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B09—DISPOSAL OF SOLID WASTE; RECLAMATION OF CONTAMINATED SOIL
- B09B—DISPOSAL OF SOLID WASTE NOT OTHERWISE PROVIDED FOR
- B09B3/00—Destroying solid waste or transforming solid waste into something useful or harmless
- B09B3/40—Destroying solid waste or transforming solid waste into something useful or harmless involving thermal treatment, e.g. evaporation
Landscapes
- Engineering & Computer Science (AREA)
- Environmental & Geological Engineering (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Processing Of Solid Wastes (AREA)
Abstract
本发明涉及一种医疗废弃物的无碳排放处理方法,采用电磁波照射医疗废弃物,在吸波材料催化剂的作用下,使医疗垃圾中有机大分子的碳碳键发生共振断键,形成有机小分子产物从反应炉中逸出,经过冷凝回收液体产物燃料油,不可冷凝气体经压缩得到液化气和不可压缩可燃气。残留的裂解固体从反应炉底部排出;整个工艺过程采用清洁能源电磁波,无任何排放,气、固、液全回收,有机物转化率100%。
Description
技术领域
本发明涉及医疗废弃物处理技术领域,具体的说是一种医疗废弃物的无碳排放处理方法。
背景技术
医疗垃圾是具有直接或间接污染性、毒性及其他危害性的废物,被列入《国家危险废物名录》。目前国际上应用较多的医疗废弃物的处理方法主要是高温焚烧处理方法。这种技术的优点是适用范围广,处理后的废物难以辨认,清毒杀菌彻底,减容减量效果显著,技术比较成熟等优点。但是,医疗废弃物的主要成份是碳氢有机化合物,高温焚烧法的结果是排放大量的CO2,尤其是不可避免的产生“世纪之毒”二噁英。随着当前国际社会对环境保护要求严格,和温室气体CO2浓度的急剧增长带来的隐患,以及普通民众对建造焚烧炉的反感,使得高温焚烧炉建设的压力越来越大,扩展和扩大规模极为困难,再加上高温焚烧法的成本高,空气污染严重,易产生二噁英、多环芳香族化合物、多氯联苯等剧毒物以及氯化氢和二氧化硫等有害气体,尤其是医疗垃圾维持燃烧,需要添加辅助燃料以提供加热垃圾达到燃烧温度所需要的热量和发生燃烧所必须的活化能,等等原因,更加使这一技术推广受到限制。医疗废弃物的另一种常用的处理方法是高压蒸汽灭菌法,这种技术的优点是投资小,操作费用低,清毒效果好,残留物危险性低。但是缺点是体积和外观基本没有改变,且易产生臭气。不能处理甲醛、苯酚及汞等物质,对病理性垃圾及药物和化学垃圾处理效率不高。还有一种医疗废弃物的处理方法是热裂解,利用医疗垃圾中的有机物的热不稳定性,在无氧或缺氧条件下对其进行加热蒸馏,使有机物产生热裂解,经冷凝后形成各种气体、液体和固体,从中提取燃料油、油脂和燃料气。医疗废弃物的热解技术,是将裂解的气体产物和固体产物作为热解供热热源的燃料,与高温焚烧法相比,所需空气系数小,产生烟气量大大减少,其运行成本也大大降低,还能得到部分可销售的油品,总体费用比高温焚烧法低。同时,产生二噁英的量也大为减少。然而,由于热解所需要的温度很高,热解产物气体、固体被全部用于燃烧供热,热裂解医疗废弃物仅仅能得到不到一半的液体产物,燃烧所排放的CO2量自然很大,不符合当今国际上碳减排的要求。其他的如微波处理技术、化学处理技术、电弧炉处理技术和等离子处理技术等,目前还处于研究阶段,实现工业化大规模处理还需要一段漫长的道路。
发明内容
针对上述现有的热裂解医疗废弃物仅仅能得到不到一半的液体产物,燃烧所排放的CO2量大,不符合当今国际上碳减排的要求等问题,本发明提供一种医疗废弃物的无碳排放处理方法。包括以下步骤:
步骤一:将经过粉碎,外形最大尺寸不超过5cm的医疗废弃物放入反应炉中,与催化剂充分混合,备用;
步骤二:用频率在1000Hz~20000Hz范围内的电磁波,照射步骤一所得的医疗废弃物,使医疗废弃物中的有机大分子发生化学键C-C键断裂,生成有机小分子;
步骤三:分解出的有机小分子产物从反应炉中逸出,经多级冷凝、压缩,可分别得到重质油组分碳链大于C18、柴油组分C10~C18、汽油组分C6~C10、轻质油组分C4~C6、液化气C2~C4及可燃气CH4、H2和CO;
步骤四:有机大分子分解的固体产物为固体碳,从反应炉的底部排出。
所述的医疗废弃物为感染性废物、病理性废物、损伤性废物、药物性废物或化学性废物,但不包括液态或气态医疗废弃物血清、血液、福尔马林液和过氧乙酸消毒液。
所述反应炉采用内外双波源发射,内外波源功率比为0.5~0.7。
所述反应炉中的波辐射时间为10~40min,反应炉内的压力在500Pa~10000Pa,反应炉内的温度为180℃~380℃。
所述有机大分子分解后的固体产物,其热值大于5500Kcal/kg,其比表面积大于100m2/g。
所述催化剂为磁性催化剂,且在1000Hz~20000Hz频率范围内有最大吸收。
本发明的有益效果:
本发明提供的医疗废弃物的无碳排放处理方法,采用电磁波照射医疗废弃物,在吸波材料催化剂的作用下,使医疗垃圾中有机大分子的碳碳键发生共振断键,形成有机小分子产物从反应炉中逸出,经过冷凝回收液体产物燃料油,不可冷凝气体经压缩得到液化气和不可压缩可燃气。残留的裂解固体从反应炉底部排出;整个工艺过程采用清洁能源电磁波,无任何排放,气、固、液全回收,有机物转化率100%;本发明得到的固体产物,由于结构中C-C化学键的断裂,使得固体产物具有较大的孔隙率和比表面积,无需处理就可以用于工业污水的吸附剂。因为反应炉内温度在180℃~385℃,可以有效起到杀菌消毒的作用,残留固体可以直接使用,而对环境无害。另外,医疗废弃物反应后的固体产物经热值仪分析,其具有5500千卡/kg的热值,完全可以代替低标号的煤使用,提供热能。
附图说明
图1 本发明实施例1液体产物液质分析谱图;
图2 本发明实施例2液体产物液质分析谱图。
具体实施方式
下面结合具体实施方式对本发明做进一步的阐述。
实施例1
医疗废弃物来源于郑州市医疗垃圾处理公司,随即选取,称取169.5g(#1),与5.5g催化剂在500mL石英圆底烧瓶充分混合均匀,放入到反应炉中反应。反应时间15分钟。裂解气体经水冷却收集液体产物,不可冷凝气体用气体流量计标定重量,反应炉中固体的重量用电子天平称重。反应后得到108.5g液体,14.5g固体和46.5g气体。液体产物用液质联用仪分析产物组成,分析数据见附图1及表1。#1的固体产物热值为5536Kcal/kg。
表1 #1液体产物的组成分析表
实施例2
医疗废弃物来源于青岛市医疗垃圾焚烧厂,随机选取,称取71.5g(#2),与2.8g催化剂在500mL石英圆底烧瓶充分混合均匀,放入到实验反应炉中反应。反应时间10分钟。裂解气体经水冷却收集液体产物,不可冷凝气体用气体流量计标定重量,反应炉中固体的重量用电子天平称重。反应后得到45.0g液体,5.0g固体和21.5g气体。液体产物用液质联用仪分析产物组成,分析数据见附图2及表2, #2的固体热值为5610Kcal/kg。
表2 #2液体产物的组成分析表
Claims (7)
1.一种医疗废弃物的无碳排放处理方法,其特征在于,包括以下步骤:
步骤一:将经过粉碎,外形最大尺寸不超过5cm的医疗废弃物放入反应炉中,催化剂与反应炉结为一体形成固定床;
步骤二:用频率在1000Hz~20000Hz范围内的电磁波,照射步骤一所得的医疗废弃物,使医疗废弃物中的有机大分子发生化学键C-C键断裂,生成有机小分子;
步骤三:分解出的有机小分子产物从反应炉中逸出,经多级冷凝、压缩,可得到四种油品、天然气和液化气;
步骤四:有机大分子分解的固体产物为固体碳,从反应炉的底部排出。
2.如权利要求1所述的医疗废弃物的无碳排放处理方法,其特征在于:所述的医疗废弃物为感染性废物、病理性废物、损伤性废物、药物性废物或化学性废物,但不包括液态或气态医疗废弃物血清、血液、福尔马林液和过氧乙酸消毒液。
3.如权利要求1所述的医疗废弃物的无碳排放处理方法,其特征在于:所述反应炉采用内外双波源发射,内外波源功率比为0.5~0.7。
4.如权利要求1所述的医疗废弃物的无碳排放处理方法,其特征在于:所述反应炉中的波辐射时间为10~40min,反应炉内的压力在500Pa~10000Pa,反应炉内的温度为180℃~380℃。
5.如权利要求1所述的医疗废弃物的无碳排放处理方法,其特征在于:所述有机大分子分解后的固体产物,其热值大于5500Kcal/kg,其比表面积大于100m2/g。
6.如权利要求1所述的医疗废弃物的无碳排放处理方法,其特征在于:所述催化剂为磁性材料,且在1000Hz~20000Hz频率范围内有最大吸收。
7.如权利要求6所述的医疗废弃物的无碳排放处理方法,其特征在于:所述磁性催化剂为铁磁性材料。
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201710771797.9A CN107520235A (zh) | 2017-08-31 | 2017-08-31 | 一种医疗废弃物的无碳排放处理方法 |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201710771797.9A CN107520235A (zh) | 2017-08-31 | 2017-08-31 | 一种医疗废弃物的无碳排放处理方法 |
Publications (1)
Publication Number | Publication Date |
---|---|
CN107520235A true CN107520235A (zh) | 2017-12-29 |
Family
ID=60683183
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201710771797.9A Withdrawn CN107520235A (zh) | 2017-08-31 | 2017-08-31 | 一种医疗废弃物的无碳排放处理方法 |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN107520235A (zh) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN111780118A (zh) * | 2020-07-21 | 2020-10-16 | 北京化工大学 | 一种医疗废弃物高效回收及利用装置 |
CN112238122A (zh) * | 2020-09-15 | 2021-01-19 | 介翔宇 | 一种医疗废弃物微波催化分解的处理工艺 |
CN112552940A (zh) * | 2020-11-19 | 2021-03-26 | 河南科技大学 | 固相法由农作物秸秆制取可燃气、生物油和活性炭的方法 |
Citations (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US20030215354A1 (en) * | 2002-05-17 | 2003-11-20 | Advanced Scientific Technologies Corporation | Systems and methods for in situ soil sterilization, insect extermination and weed killing |
CN103071442A (zh) * | 2011-10-25 | 2013-05-01 | 青岛东方循环能源有限公司 | 波裂解大分子有机物的方法 |
CN103172903A (zh) * | 2011-11-15 | 2013-06-26 | 青岛东方循环能源有限公司 | 电磁裂解方法及其装置 |
CN103203211A (zh) * | 2013-03-25 | 2013-07-17 | 青岛东方循环能源有限公司 | 波裂解含碳-碳单键有机物的方法 |
CN103459768A (zh) * | 2011-04-04 | 2013-12-18 | 哈里公司 | 使用射频电磁波加工烃 |
CN106475395A (zh) * | 2016-09-12 | 2017-03-08 | 河南光解环保科技有限公司 | 固体废弃物无害化、资源化处理方法以及处理装置 |
-
2017
- 2017-08-31 CN CN201710771797.9A patent/CN107520235A/zh not_active Withdrawn
Patent Citations (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US20030215354A1 (en) * | 2002-05-17 | 2003-11-20 | Advanced Scientific Technologies Corporation | Systems and methods for in situ soil sterilization, insect extermination and weed killing |
CN103459768A (zh) * | 2011-04-04 | 2013-12-18 | 哈里公司 | 使用射频电磁波加工烃 |
CN103071442A (zh) * | 2011-10-25 | 2013-05-01 | 青岛东方循环能源有限公司 | 波裂解大分子有机物的方法 |
CN103172903A (zh) * | 2011-11-15 | 2013-06-26 | 青岛东方循环能源有限公司 | 电磁裂解方法及其装置 |
CN103203211A (zh) * | 2013-03-25 | 2013-07-17 | 青岛东方循环能源有限公司 | 波裂解含碳-碳单键有机物的方法 |
CN106475395A (zh) * | 2016-09-12 | 2017-03-08 | 河南光解环保科技有限公司 | 固体废弃物无害化、资源化处理方法以及处理装置 |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN111780118A (zh) * | 2020-07-21 | 2020-10-16 | 北京化工大学 | 一种医疗废弃物高效回收及利用装置 |
CN112238122A (zh) * | 2020-09-15 | 2021-01-19 | 介翔宇 | 一种医疗废弃物微波催化分解的处理工艺 |
CN112552940A (zh) * | 2020-11-19 | 2021-03-26 | 河南科技大学 | 固相法由农作物秸秆制取可燃气、生物油和活性炭的方法 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
Harussani et al. | Pyrolysis of polypropylene plastic waste into carbonaceous char: Priority of plastic waste management amidst COVID-19 pandemic | |
CN107520235A (zh) | 一种医疗废弃物的无碳排放处理方法 | |
CN1769397A (zh) | 利用热解气化处理技术抑制垃圾尾气有害物的装置与方法 | |
Zhang et al. | TG-MS analysis and kinetic study for thermal decomposition of six representative components of municipal solid waste under steam atmosphere | |
Liu et al. | Formation of environmentally persistent free radicals during thermochemical processes and their correlations with unintentional persistent organic pollutants | |
US8283512B1 (en) | Method and system for enhanced energy production from transforming, reducing and eliminating organic material and medical wastes | |
CN106475395B (zh) | 固体废弃物无害化、资源化处理方法以及处理装置 | |
JP2007246867A (ja) | 有機性廃棄物の資源化回収装置 | |
Liu et al. | Technical and environmental feasibility of gas-solid decontamination by oxygen-enriched co-combustion of textile dyeing sludge and durian shell | |
Truong et al. | Mechanisms of molecular product and persistent radical formation from the pyrolysis of hydroquinone | |
CN110272762A (zh) | 一种co2与亚/超临界水协同作用气化污泥的方法 | |
Naveed et al. | A comparative study of gasification of food waste (FW), poultry waste (PW), municipal solid waste (MSW) and used tires (UT) | |
Zhang et al. | Incineration experiment of medical waste of novel coronavirus pneumonia (COVID-19) in a mobile animal carcass incinerator | |
Oh et al. | Dehydrochlorination characteristics of waste PVC wires by thermal decomposition | |
Song et al. | Comprehensive insight into co-pyrolysis of sewage sludge and tobacco stalk: Effects of mixing ratio and pyrolysis conditions on product distribution and characteristics | |
KR101450468B1 (ko) | 브라운가스의 열융합특성을 이용한 워터에너지 무연소각기 | |
CN102536460A (zh) | 等离子体废热电能循环利用方法及系统 | |
CN106111663B (zh) | 一种工业固体废弃物的热解气化方法 | |
Yu et al. | Enhancement of H2 and light oil production and CO2 emission mitigation during co-pyrolysis of oily sludge and incineration fly ash | |
Sánchez et al. | Pilot scale thermolysis of municipal solid waste: Combustibility of the products of the process and gas cleaning treatment of the combustion gases | |
US8512215B2 (en) | Method for enhanced energy production from transforming, reducing and eliminating organic material and medical waste | |
Li et al. | Effects of atmosphere and blending ratios on emission characteristics of pollutants from co‐combustion of municipal solid waste and aged refuse | |
CN106390939B (zh) | 一种重金属离子吸附剂 | |
CN106433706B (zh) | 一种耐高温水汽环境的蒸馏炭化装置 | |
CN111637462A (zh) | 一种医疗废物的热解焚烧方法 |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
PB01 | Publication | ||
PB01 | Publication | ||
SE01 | Entry into force of request for substantive examination | ||
SE01 | Entry into force of request for substantive examination | ||
WW01 | Invention patent application withdrawn after publication |
Application publication date: 20171229 |
|
WW01 | Invention patent application withdrawn after publication |