CN101215488A - Solid fuel mixed with organic waste and sludge and preparation method thereof - Google Patents
Solid fuel mixed with organic waste and sludge and preparation method thereof Download PDFInfo
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- CN101215488A CN101215488A CNA2008100520693A CN200810052069A CN101215488A CN 101215488 A CN101215488 A CN 101215488A CN A2008100520693 A CNA2008100520693 A CN A2008100520693A CN 200810052069 A CN200810052069 A CN 200810052069A CN 101215488 A CN101215488 A CN 101215488A
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- 239000004449 solid propellant Substances 0.000 title claims abstract description 45
- 239000010815 organic waste Substances 0.000 title claims abstract description 33
- 238000002360 preparation method Methods 0.000 title claims abstract description 19
- 239000010802 sludge Substances 0.000 title abstract description 50
- 239000003245 coal Substances 0.000 claims abstract description 28
- 239000003795 chemical substances by application Substances 0.000 claims abstract description 17
- 238000006477 desulfuration reaction Methods 0.000 claims abstract description 17
- 230000023556 desulfurization Effects 0.000 claims abstract description 17
- 239000000446 fuel Substances 0.000 claims abstract description 12
- 238000000465 moulding Methods 0.000 claims abstract description 10
- 239000002245 particle Substances 0.000 claims description 25
- 239000000203 mixture Substances 0.000 claims description 24
- 238000001035 drying Methods 0.000 claims description 22
- 238000000034 method Methods 0.000 claims description 21
- 239000002893 slag Substances 0.000 claims description 7
- 239000011449 brick Substances 0.000 claims description 6
- 229910001385 heavy metal Inorganic materials 0.000 claims description 5
- 230000008569 process Effects 0.000 claims description 4
- 238000002156 mixing Methods 0.000 claims description 3
- 238000007605 air drying Methods 0.000 claims description 2
- 230000000382 dechlorinating effect Effects 0.000 claims 3
- 239000002817 coal dust Substances 0.000 claims 2
- 238000000748 compression moulding Methods 0.000 claims 2
- 239000000306 component Substances 0.000 claims 1
- 230000018044 dehydration Effects 0.000 claims 1
- 238000006297 dehydration reaction Methods 0.000 claims 1
- 235000011194 food seasoning agent Nutrition 0.000 claims 1
- 239000010813 municipal solid waste Substances 0.000 abstract description 35
- 238000002485 combustion reaction Methods 0.000 abstract description 22
- 238000006298 dechlorination reaction Methods 0.000 abstract description 15
- 239000000843 powder Substances 0.000 abstract description 14
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 abstract description 14
- 239000002994 raw material Substances 0.000 abstract description 11
- 238000007596 consolidation process Methods 0.000 abstract description 5
- 230000007613 environmental effect Effects 0.000 abstract description 4
- 238000004519 manufacturing process Methods 0.000 abstract description 3
- 239000002803 fossil fuel Substances 0.000 abstract description 2
- 239000002699 waste material Substances 0.000 description 33
- 238000007654 immersion Methods 0.000 description 11
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 7
- 229910052717 sulfur Inorganic materials 0.000 description 7
- 239000011593 sulfur Substances 0.000 description 7
- 239000010791 domestic waste Substances 0.000 description 5
- 239000004033 plastic Substances 0.000 description 5
- 229920003023 plastic Polymers 0.000 description 5
- 239000010865 sewage Substances 0.000 description 5
- 230000000694 effects Effects 0.000 description 4
- 238000000691 measurement method Methods 0.000 description 4
- 239000004484 Briquette Substances 0.000 description 3
- 230000008859 change Effects 0.000 description 3
- 230000029087 digestion Effects 0.000 description 3
- 238000004064 recycling Methods 0.000 description 3
- 238000004056 waste incineration Methods 0.000 description 3
- 241000894006 Bacteria Species 0.000 description 2
- ZAMOUSCENKQFHK-UHFFFAOYSA-N Chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 description 2
- 239000002956 ash Substances 0.000 description 2
- 239000011230 binding agent Substances 0.000 description 2
- 239000000460 chlorine Substances 0.000 description 2
- 229910052801 chlorine Inorganic materials 0.000 description 2
- 238000011161 development Methods 0.000 description 2
- 238000001599 direct drying Methods 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 238000011156 evaluation Methods 0.000 description 2
- 239000000295 fuel oil Substances 0.000 description 2
- 239000007789 gas Substances 0.000 description 2
- NUJOXMJBOLGQSY-UHFFFAOYSA-N manganese dioxide Chemical compound O=[Mn]=O NUJOXMJBOLGQSY-UHFFFAOYSA-N 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 238000000197 pyrolysis Methods 0.000 description 2
- 230000009467 reduction Effects 0.000 description 2
- 239000007787 solid Substances 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- 231100000331 toxic Toxicity 0.000 description 2
- 230000002588 toxic effect Effects 0.000 description 2
- 239000002351 wastewater Substances 0.000 description 2
- 241001148470 aerobic bacillus Species 0.000 description 1
- 238000003915 air pollution Methods 0.000 description 1
- 238000004458 analytical method Methods 0.000 description 1
- 239000012298 atmosphere Substances 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 244000052616 bacterial pathogen Species 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000003763 carbonization Methods 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 239000010883 coal ash Substances 0.000 description 1
- 238000009264 composting Methods 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 150000002013 dioxins Chemical class 0.000 description 1
- 201000010099 disease Diseases 0.000 description 1
- 208000037265 diseases, disorders, signs and symptoms Diseases 0.000 description 1
- 238000009826 distribution Methods 0.000 description 1
- 239000000428 dust Substances 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 239000003623 enhancer Substances 0.000 description 1
- 238000003912 environmental pollution Methods 0.000 description 1
- 238000002474 experimental method Methods 0.000 description 1
- 239000004744 fabric Substances 0.000 description 1
- 238000000855 fermentation Methods 0.000 description 1
- 230000004151 fermentation Effects 0.000 description 1
- 230000036541 health Effects 0.000 description 1
- 230000006872 improvement Effects 0.000 description 1
- 238000004898 kneading Methods 0.000 description 1
- QSHDDOUJBYECFT-UHFFFAOYSA-N mercury Chemical compound [Hg] QSHDDOUJBYECFT-UHFFFAOYSA-N 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 244000005700 microbiome Species 0.000 description 1
- 235000015097 nutrients Nutrition 0.000 description 1
- 239000003921 oil Substances 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 239000000123 paper Substances 0.000 description 1
- 239000010893 paper waste Substances 0.000 description 1
- 238000001556 precipitation Methods 0.000 description 1
- 238000003825 pressing Methods 0.000 description 1
- 238000012545 processing Methods 0.000 description 1
- 239000000779 smoke Substances 0.000 description 1
- 239000002689 soil Substances 0.000 description 1
- 239000002910 solid waste Substances 0.000 description 1
- 238000009270 solid waste treatment Methods 0.000 description 1
- 238000007619 statistical method Methods 0.000 description 1
- 239000002341 toxic gas Substances 0.000 description 1
- 239000002023 wood Substances 0.000 description 1
Classifications
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- 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
- Y02E50/00—Technologies for the production of fuel of non-fossil origin
- Y02E50/30—Fuel from waste, e.g. synthetic alcohol or diesel
Landscapes
- Solid Fuels And Fuel-Associated Substances (AREA)
Abstract
本发明公开了一种有机垃圾与污泥混合的固体燃料及其制备方法。固体燃料包括有机垃圾:25%~55%,污泥:20%~50%,煤粉:20%~50%,助燃剂:0.15%~0.25%,脱硫脱氯剂:0.5%~2%。其制备过程包含原料制备、成型、固结3个阶段。本发明经固体燃料机械强度、燃烧特性、污染控制等测试。本发明制造方法得到的有机垃圾与污泥混合的固体燃料是一种较理想的洁净燃料,具有较高的机械强度,满足远距离运输,落下强度达99%以上,是一种具有机械性能强、耐水性好、燃烧特性优、热稳定性强的无污染固体燃料,可以推广至民用及工业部门应用。并能节省大量石油,煤炭等不可再生的化石燃料,具有良好的社会和环境效益。The invention discloses a solid fuel mixed with organic garbage and sludge and a preparation method thereof. Solid fuel includes organic waste: 25% to 55%, sludge: 20% to 50%, coal powder: 20% to 50%, combustion accelerant: 0.15% to 0.25%, desulfurization and dechlorination agent: 0.5% to 2%. The preparation process includes three stages: raw material preparation, molding and consolidation. The invention has been tested on solid fuel mechanical strength, combustion characteristics, pollution control and the like. The solid fuel mixed with organic garbage and sludge obtained by the manufacturing method of the present invention is an ideal clean fuel, has high mechanical strength, meets long-distance transportation, and has a drop strength of more than 99%. It is a kind of solid fuel with strong mechanical properties. , non-polluting solid fuel with good water resistance, excellent combustion characteristics, and strong thermal stability can be extended to civil and industrial applications. And it can save a lot of non-renewable fossil fuels such as oil and coal, and has good social and environmental benefits.
Description
【技术领域】【Technical field】
本发明涉及生活垃圾、污泥资源化利用和环保能源技术领域,特别是一种能够对城市生活垃圾减量化、无害化、资源化处理的有机垃圾与污泥混合的固体燃料及其制备方法。The invention relates to the technical field of domestic garbage and sludge resource utilization and environmental protection energy, in particular to a solid fuel capable of reducing, harmless and resourceful treatment of urban domestic garbage mixed with organic garbage and sludge and its preparation method.
【背景技术】【Background technique】
我国仅“城市垃圾”的年产量就近1.5亿吨,并以7%~9%年递增速度增加。据不完全统计,中国城市生活垃圾的历年堆存置达60多亿吨,约有2/3的城市陷入垃圾围城的困境。城市垃圾绝大部分是露天堆放,不仅影响城市景观,同时污染了与我们生命至关重要的大气、水和土壤,对城镇居民的健康构成威胁。垃圾已成为城市发展中的棘手问题。现有处理生活垃圾的方法除露天堆放外,还有卫生填埋。卫生填埋虽避免了露天堆放产生的问题,但填埋场占地面积大,使用时间短(一般十年左右),造价高,同时垃圾中可利用的资源没有得到回收。此外,垃圾处理还有一种方法是焚烧。垃圾焚烧可使垃圾体积缩小50%~95%,但焚烧的同时也烧掉了可回收的资源,释放出有毒气体,如二噁英、电池中的汞蒸汽等,并产生有毒有害炉渣和灰尘。至于堆肥方法则需先将有机垃圾与其它垃圾分开才行。现有的这些垃圾处理方法还都需要高额的处理费用。处理一吨垃圾花费一般上百元,这还不包括建设垃圾处理场的费用,如建一座大型垃圾填埋厂需1~2亿元,建一座大型垃圾焚烧厂需20多亿元。一座城市垃圾焚烧厂,不计征地和炉渣处理的费用,规模1000吨/日焚烧厂的投资都在7亿元人民币以上,而平均运行费为70~150元/吨垃圾。The annual output of "urban waste" in my country alone is nearly 150 million tons, and it is increasing at an annual rate of 7% to 9%. According to incomplete statistics, China's urban domestic waste has been piled up to more than 6 billion tons over the years, and about two-thirds of the cities are trapped in the predicament of garbage siege. The vast majority of urban waste is piled in the open air, which not only affects the urban landscape, but also pollutes the atmosphere, water and soil that are vital to our lives, posing a threat to the health of urban residents. Garbage has become a thorny problem in urban development. Existing methods for dealing with domestic waste include sanitary landfill except open-air stacking. Although sanitary landfill avoids the problems caused by open-air stacking, the landfill covers a large area, is used for a short period of time (usually about ten years), and is expensive. At the same time, the resources available in the garbage have not been recycled. In addition, another method of garbage disposal is incineration. Garbage incineration can reduce the volume of garbage by 50% to 95%, but at the same time, it also burns recyclable resources, releases toxic gases, such as dioxins, mercury vapor in batteries, etc., and produces toxic and harmful slag and dust . As for the composting method, it is necessary to separate the organic waste from other waste. These existing garbage disposal methods also all need high treatment costs. Disposing of a ton of waste generally costs hundreds of yuan, not including the cost of building a waste disposal site. For example, it takes 100-200 million yuan to build a large-scale waste landfill plant, and more than 2 billion yuan to build a large-scale waste incineration plant. For an urban waste incineration plant, excluding the cost of land acquisition and slag treatment, the investment of a 1,000-ton/day incineration plant is more than 700 million yuan, and the average operating cost is 70-150 yuan/ton of waste.
我国城市垃圾的平均低位热值只有约600kcal/kg,低于国家规定的1000kcal/kg入炉垃圾最低热值标准。目前,全世界对低热值垃圾还没有很好的焚烧方法,而垃圾燃烧不充分导致外排的浓烟夹带着大量剧毒和有害物质,严重地污染了环境。The average low calorific value of urban waste in my country is only about 600kcal/kg, which is lower than the minimum calorific value standard of 1000kcal/kg for furnace waste stipulated by the state. At present, there is no good incineration method for low-calorific-value garbage in the world, and the insufficient combustion of garbage causes a large amount of highly toxic and harmful substances in the exhausted smoke, which seriously pollutes the environment.
而当前大量未经分类就填埋或焚烧的垃圾,既是对资源的巨大浪费,又会产生二次污染。生活垃圾中可直接回收利用物质不低于33%,每年年产1.5亿吨的城市垃圾中,被丢弃的“可再生资源”价值高达250亿元!At present, a large amount of garbage that is landfilled or incinerated without classification is not only a huge waste of resources, but also produces secondary pollution. Not less than 33% of domestic waste can be directly recycled. Among the annual output of 150 million tons of urban waste, the value of discarded "renewable resources" is as high as 25 billion yuan!
城市生活垃圾为多种物质混合而成的复杂体,由煤灰、砖瓦、纸张、塑料、金属、橱余、木屑等废弃物组成。其组分主要受城市发展规模、气候、季节、生活水平与习惯、能源结构等影响。随着居民生活水平的提高,食品结构的变化,尤其是能源结构的改变,城市生活垃圾的构成发生了明显的变化,有机可燃成分含量低、无机不可燃成分含量高、垃圾成分波动大;水分含量高、热值较低,难以直接实现能源化,垃圾资源化利用率低。Municipal solid waste is a complex mixture of various substances, consisting of coal ash, bricks, paper, plastics, metal, cabinet waste, wood chips and other wastes. Its components are mainly affected by the scale of urban development, climate, seasons, living standards and habits, and energy structure. With the improvement of residents' living standards and the change of food structure, especially the change of energy structure, the composition of municipal solid waste has undergone obvious changes, with low content of organic combustible components, high content of inorganic non-combustible components, and large fluctuations in garbage components; moisture content With high content and low calorific value, it is difficult to directly realize energy conversion, and the utilization rate of waste resources is low.
除了城市生活垃圾处理的难题外,我国城市污水处理厂每年排放的污泥量(干重)大约为130万吨,并以10~20%的速度递增。特别是在我国城市化水平较高的几个城市与地区,污泥出路问题已经十分突出。如果城市污水全部得到处理,则将产生污泥量(干重)为840万吨,占我国总固体废弃物的3.2%。如何处置这么大量的污泥,这是许多大城市都将面临的问题。国内主要污泥处理方式主要有填埋法、焚烧法、直接烘干法、厌氧消化法、生物处理法。填埋法基本类似于城市垃圾填埋,要占用大量土地,浪费土地资源;而污泥中含有的营养物质使大量病杂菌繁衍,导致污泥霉变,污染环境,据国内污水处理厂调查,每吨污泥的填埋处理费用平均约40元/吨;现有的污泥焚烧需要耗费大量重油而不经济,并造成大气污染,浪费资源。如在日本污泥焚烧处理占污泥处理总量的60%以上,焚烧工艺大部分采用多段焚烧炉,一套处理量50m3/d左右的焚烧设备成本高达28亿日元;直接烘干法可将含水率75%~80%的污泥烘干,温度高达200℃以上,杀死各种病菌,然后进行填埋或再处理,但能耗高,处理成本高;80年代以前大多数的活性污泥采用厌氧消化法处理,杀灭微生物病菌并生产部分可利用的沼气。有关资料显示,污泥厌氧消化系统的建设投资约为100~200万元/吨干泥,运行费用大约700~900元/吨干泥;生物处理法即生物堆肥法,它是引进好氧菌种和氧气,使污泥好氧生物高温发酵。目前我国污泥处理处置主要方法中污泥农用约占44.8%、陆地填埋约占31%、其它处置约10.5%、没有处置约13.7%,据统计,我国用于污泥处理处置的投资约占污水处理厂总投资的20~50%,污泥处理处置处于严重滞后状态。In addition to the difficult problem of municipal solid waste treatment, the amount of sludge (dry weight) discharged by my country's urban sewage treatment plants is about 1.3 million tons per year, and it is increasing at a rate of 10-20%. Especially in several cities and regions with a high level of urbanization in my country, the problem of sludge outlets has become very prominent. If all urban sewage is treated, the amount of sludge (dry weight) will be 8.4 million tons, accounting for 3.2% of the total solid waste in my country. How to dispose of such a large amount of sludge is a problem that many big cities will face. The main domestic sludge treatment methods mainly include landfill, incineration, direct drying, anaerobic digestion, and biological treatment. The landfill method is basically similar to urban waste landfill, which takes up a lot of land and wastes land resources; while the nutrients contained in the sludge cause a large number of disease and miscellaneous bacteria to multiply, resulting in mildew in the sludge and polluting the environment. According to the survey of domestic sewage treatment plants , The average cost of landfill treatment per ton of sludge is about 40 yuan/ton; the existing sludge incineration needs to consume a lot of heavy oil, which is not economical, and causes air pollution and wastes resources. For example, in Japan, sludge incineration accounts for more than 60% of the total sludge treatment, and most of the incineration processes use multi-stage incinerators. The cost of a set of incineration equipment with a processing capacity of about 50m3/d is as high as 2.8 billion yen; direct drying method can Dry the sludge with a moisture content of 75% to 80%, and the temperature is as high as 200°C to kill various germs, and then landfill or reprocess, but the energy consumption is high and the treatment cost is high; most of the active sludge before the 1980s Sludge is treated by anaerobic digestion to kill microorganisms and bacteria and produce some usable biogas. Relevant data show that the construction investment of the sludge anaerobic digestion system is about 1 to 2 million yuan/ton of dry mud, and the operating cost is about 700 to 900 yuan/ton of dry mud; the biological treatment method is the biocomposting method, which is the introduction of aerobic Bacteria and oxygen make sludge aerobic biological high-temperature fermentation. At present, the main methods of sludge treatment and disposal in my country account for about 44.8% for agricultural use, about 31% for landfill, about 10.5% for other disposal, and about 13.7% for non-disposal. According to statistics, the investment in sludge treatment and disposal in my country is about Accounting for 20-50% of the total investment of sewage treatment plants, sludge treatment and disposal are in a serious lagging state.
国内的垃圾热值低、水分高、变化大、分选难、产量世界第一,这个现实在短时间内难以改变。在垃圾现状、经济和技术三大制约因素的重重包围中,如何充分利用垃圾资源,开发出具有我国自主知识产权的低热值垃圾资源化高效利用技术已成当务之急。如北京市现日产垃圾13000吨,全年生产495万吨,其中废塑料36.2万吨,废纸38.8万吨,废食品草木121.3万吨,且每年将以8%的速度递增,若将这些有机垃圾作为燃料资源,则能带来巨大的经济效益。Domestic waste has low calorific value, high moisture content, large changes, difficult sorting, and the world's largest output. This reality is difficult to change in a short period of time. Surrounded by the three major constraints of waste status, economy and technology, how to make full use of waste resources and develop low calorific value waste resource efficient utilization technologies with my country's independent intellectual property rights has become a top priority. For example, Beijing currently produces 13,000 tons of garbage per day, with an annual output of 4.95 million tons, including 362,000 tons of waste plastics, 388,000 tons of waste paper, and 1.213 million tons of waste food and vegetation, and will increase at an annual rate of 8%. Garbage as a fuel resource can bring huge economic benefits.
【发明内容】【Content of invention】
本发明的目的是针对现有城市垃圾中可回收资源的巨大浪费,以及垃圾焚烧处理高额费用的问题,提供一种有机垃圾与污泥混合的固体燃料及其制备方法,该固体燃料使用有机垃圾作为原料主成分,水溶性的废水污泥作为粘结剂,实现固体有机废物的资源化、无害化、减量化处理。The purpose of the present invention is to provide a solid fuel mixed with organic waste and sludge and its preparation method for the huge waste of recyclable resources in the existing urban waste and the high cost of waste incineration. Garbage is used as the main component of raw materials, and water-soluble wastewater sludge is used as a binder to realize the recycling, harmless and reduction treatment of solid organic waste.
本发明为实现上述目的公开了一种有机垃圾与污泥混合的固体燃料。其特征在于所述燃料包括有机垃圾,污泥,煤粉混配组成,所述各种成分的重量百分比是:有机垃圾:25%~55%,污泥:20%~50%,煤粉:20%~50%,助燃剂:0.15%~0.25%,脱硫脱氯剂:0.5%~2%。The invention discloses a solid fuel mixed with organic garbage and sludge to achieve the above purpose. It is characterized in that the fuel is composed of organic waste, sludge and coal powder, and the weight percentages of the various components are: organic waste: 25% to 55%, sludge: 20% to 50%, coal powder: 20% to 50%, combustion enhancer: 0.15% to 0.25%, desulfurization and dechlorination agent: 0.5% to 2%.
所述助燃剂可以是:MnO2或KMnO4中的一种或混合物。The combustion aid can be one or a mixture of MnO 2 or KMnO 4 .
所述脱硫脱氯剂可以是:CaO或CaCO3、MgO中的一种或混合物。The desulfurization and dechlorination agent can be: CaO or one or a mixture of CaCO 3 and MgO.
本发明还公开了一种有机垃圾与污泥混合的固体燃料的制备方法,其特征在于包括以下步骤:将除去了重金属和砖渣、瓦片等无机成分的有机垃圾经干燥脱水,将有机垃圾和煤分别破碎至3mm~10mm粒径,再将有机垃圾颗粒、煤粉颗粒、污泥、助燃剂和脱硫脱氯剂按比例充分混合,适宜的水分含量为8%~12%;经机械或人工混捏,压制成型;将成型产品自然干燥至水分含量5%~15%。The invention also discloses a method for preparing solid fuel mixed with organic waste and sludge, which is characterized in that it comprises the following steps: drying and dehydrating the organic waste from which inorganic components such as heavy metals, brick slag, and tiles have been removed; Separately crush the coal and coal to a particle size of 3mm-10mm, and then fully mix the organic waste particles, coal powder particles, sludge, combustion accelerant and desulfurization and dechlorination agent in proportion, and the suitable moisture content is 8%-12%. Manual kneading, pressing and molding; natural drying of the shaped product to a moisture content of 5% to 15%.
本发明的有益效果是:本发明将生活垃圾作为燃料资源,通过降低水分含量,提高可燃成分含量,并将有机垃圾、污泥、高热值煤粉等经优化配比制备固体燃料。该固体燃料能达到最佳热效率,城市垃圾和污泥同时减容。本发明制作方法简单,处理费用低廉,无二次污染,并可在短期内获得经济效益,实现固体有机废物的资源化、无害化、减量化。经对256个实验结果采用统计分析、数量化理论分析方法,以及水平效应和工程效应评估等手段评价确定,用本发明制造方法得到的有机垃圾与污泥混合的固体燃料是一种较理想的洁净燃料,具有较高的机械强度,完全可以满足远距离运输,落下强度达99%以上,具有较强的耐潮、抗水性能;燃烧热值达到普通燃料利用的热值要求,热稳定性程度高,可以成为普通煤燃料的替代品,是一种具有机械性能强、耐水性好、燃烧特性优、热稳定性强,且无二次污染的固体燃料。可以推广至民用及工业部门应用,实现垃圾的资源化,减量化,无害化,做到垃圾的再生利用,可以节省大量石油,煤炭等不可再生的化石燃料,具有良好的社会和环境效益。并对令人头痛的污泥直接处理和利用,既解决废水污泥的环境污染问题,又化废为宝,提供能源,具有重要的经济和社会应用价值。The beneficial effect of the invention is that: the invention uses domestic garbage as a fuel resource, increases the content of combustible components by reducing the water content, and prepares solid fuel by optimizing the ratio of organic garbage, sludge, high calorific value coal powder, and the like. The solid fuel can achieve the best thermal efficiency, and the urban waste and sludge volume can be reduced at the same time. The preparation method of the invention is simple, the treatment cost is low, there is no secondary pollution, economic benefits can be obtained in a short period of time, and the solid organic waste can be recycled, harmless and reduced. Through adopting statistical analysis, quantitative theoretical analysis method to 256 experimental results, and means evaluation such as level effect and engineering effect evaluation, it is a kind of more ideal solid fuel that the organic refuse that obtains with the present invention's manufacturing method is mixed with sludge Clean fuel, with high mechanical strength, can fully meet the long-distance transportation, the drop strength is over 99%, and has strong moisture resistance and water resistance; the combustion calorific value meets the calorific value requirements of ordinary fuel utilization, and the degree of thermal stability High, can be a substitute for ordinary coal fuel, is a solid fuel with strong mechanical properties, good water resistance, excellent combustion characteristics, strong thermal stability, and no secondary pollution. It can be extended to civil and industrial applications to realize the recycling, reduction and harmlessness of garbage, and the recycling of garbage, which can save a lot of non-renewable fossil fuels such as oil and coal, and has good social and environmental benefits . And the troublesome sludge is directly treated and utilized, which not only solves the environmental pollution problem of wastewater sludge, but also turns waste into wealth and provides energy, which has important economic and social application value.
【具体实施方式】【Detailed ways】
本发明所采取的方案:先除去垃圾中重金属和大块砖渣、瓦片等无机成分,即为有机垃圾主要原料,其中包含了如织物、塑料等不易自然降解的可燃有机成分,经破碎、干燥,将煤粉、污泥以及脱硫脱氯剂为辅料,掺入经预处理的有机垃圾中,按一定的组分配比在湿润状态下混合搅拌后压制成一定强度和形状的固体燃料产品,经优化配比获得最佳配方,制成的产品可供民用或企业使用。The scheme adopted by the present invention: first remove heavy metals and inorganic components such as large brick slag and tiles in the garbage, which is the main raw material of organic garbage, which contains combustible organic components that are not easy to degrade naturally such as fabrics and plastics. Drying, coal powder, sludge and desulfurization and dechlorination agents are used as auxiliary materials, mixed into the pretreated organic waste, mixed and stirred in a wet state according to a certain component distribution ratio, and then pressed into a solid fuel product with a certain strength and shape. The best formula is obtained by optimizing the ratio, and the finished product can be used by civilians or enterprises.
本发明的制备过程涉及原料制备、成型、固结3个阶段。The preparation process of the present invention involves three stages of raw material preparation, molding and consolidation.
所述制备原料,包括原料的干燥、粉碎及混合。由于收集的生活垃圾含水率高,为了满足成型燃料的水分要求,除去了重金属和大块砖渣、瓦片等无机成分的有机垃圾经烘干或自然风干脱水,并将其水分含量控制在4%~8%;然后将煤粉、经干燥处理的生活垃圾采用普通的粉碎机械破碎至3mm~10mm的颗粒;再将垃圾颗粒、煤粉、污泥、助燃剂、脱硫脱氯剂按适当比例充分混合,为使原料颗粒表面均匀地被污泥所润湿、覆盖垃圾和煤粒表面,达到最佳粘结效果,并使助燃剂、脱硫脱氯剂等分布均匀,便于原料成型,适宜的水分含量为8%~12%。The preparation of raw materials includes drying, crushing and mixing of raw materials. Due to the high moisture content of the collected domestic waste, in order to meet the moisture requirements of the briquette fuel, the organic waste that has removed heavy metals, large brick slag, tiles and other inorganic components is dried or dehydrated by natural air drying, and its moisture content is controlled at 4 % to 8%; then the pulverized coal and the dried household garbage are crushed into particles of 3mm to 10mm by ordinary crushing machinery; Fully mixed, in order to make the surface of the raw material particles evenly wetted by the sludge, cover the surface of the garbage and coal particles, achieve the best bonding effect, and make the combustion improver, desulfurization and dechlorination agent, etc. evenly distributed, which is convenient for raw material molding, suitable The moisture content is 8% to 12%.
所述成型过程为第二阶段,将制备的原料采用机械或人工混捏后,在常温、常压下送入成型机(成型压力1961~3432N/cm2)压制成所需形状的固体燃料产品。The molding process is the second stage. After the prepared raw materials are mechanically or manually kneaded, they are sent to a molding machine at normal temperature and pressure (molding pressure 1961-3432N/cm 2 ) to be pressed into solid fuel products of desired shape.
第三阶段为固结过程,将成型样品自然干燥至水分含量5%~15%即可。The third stage is the consolidation process, in which the molded samples are naturally dried to a moisture content of 5% to 15%.
本发明的方案在制备时,所提供的垃圾原料仅须拣出重金属和大块砖渣、瓦片等无机成分,依靠人工或机械很容易解决,其主要成分为有机垃圾。对废塑料不必分拣出加热聚缩,干燥时不须热解或干馏·炭化,仅自然干燥即可满足制备条件。因废塑料和其它垃圾处理方法难以处理的高热值可燃物比重提高,有效地解决了因低热值垃圾成分阻碍成品燃料热值提高的根本问题。可燃成分高,可节约大量助燃油或煤,污泥为水性粘结剂,具有良好的粘结力,易于均匀混捏;该固体燃料的成型操作简便,只需常温、常压,使用一般的成型机械即可制得产品,供居民及工业等广泛使用。因此该发明无论在原料制备过程还是成型、固结过程,操作均十分简便,燃料可充分燃烧,无SO2、HCl等污染性气体造成的二次污染问题。During the preparation of the solution of the present invention, the provided garbage materials only need to sort out inorganic components such as heavy metals, large brick slag, tiles, etc., which can be easily solved manually or mechanically, and the main components are organic garbage. Waste plastics do not need to be sorted out and heat polycondensed, and there is no need for pyrolysis or dry distillation and carbonization during drying, and only natural drying can meet the preparation conditions. The proportion of high calorific value combustibles that are difficult to handle due to waste plastics and other waste treatment methods has increased, effectively solving the fundamental problem that the low calorific value of waste components hinders the increase in the calorific value of finished fuels. The combustible content is high, which can save a lot of fuel oil or coal. The sludge is a water-based binder, which has good cohesive force and is easy to knead evenly. Products can be produced by machinery, which can be widely used by residents and industries. Therefore, no matter in the process of raw material preparation or molding and consolidation, the invention is easy to operate, the fuel can be fully burned, and there is no secondary pollution caused by polluting gases such as SO 2 and HCl.
我国城市垃圾的平均低位热值只有约600kcal/kg,自身热能不足以燃烧,需要对原生垃圾进行降水提(热)值或引入经济的、数倍于垃圾自身热值的外部热能等措施才能使垃圾稳定燃烧并符合经济和环保的要求。本发明则提供了可以充分利用有机可燃垃圾和污泥(来源于城市污水处理场的污泥),经原料制备、成型、固结过程制造固体燃料及其制备方法,该发明提供的产品机械性能、燃烧特性以及热稳定性均达到型煤的技术指标。The average low-level calorific value of urban waste in my country is only about 600kcal/kg, and its own heat energy is not enough to burn. It is necessary to increase the (heat) value of the original waste by precipitation or introduce economical external heat energy that is several times the heat value of the waste itself. Garbage burns stably and meets economic and environmental requirements. The present invention provides organic combustible garbage and sludge (sludge from urban sewage treatment plants) that can be fully utilized to manufacture solid fuel and its preparation method through raw material preparation, molding, and consolidation processes. The mechanical properties of the product provided by the invention , combustion characteristics and thermal stability all meet the technical indicators of briquette.
本发明通过实施例对燃料的燃烧特性,热稳定性,以及抗压强度、落下强度、浸水强度、复干强度等机械性能指标进行了实验。In the present invention, experiments are carried out on the fuel's combustion characteristics, thermal stability, and mechanical performance indicators such as compressive strength, drop strength, water immersion strength, and re-dry strength.
[实施例1][Example 1]
将烘干后水分含量为4%~8%的有机垃圾颗粒、污泥、煤粉颗粒按1∶1∶2比例混合,加入助燃剂MnO2含量为0.18%,脱硫脱氯剂CaO含量为0.90%,混合均匀,保持水分含量为8%~12%;然后混捏加工成型,再经自然干燥至水分含量为5%~15%的固体燃料产品。采用《工业型煤冷压强度测定方法》(MT/T748-1997)测定该固体燃料的抗压强度,经测定该固体燃料的抗压强度在167.2620kPa~207.0788kPa范围,可靠性为95%。Mix organic waste particles, sludge, and coal powder particles with a moisture content of 4% to 8% after drying in a ratio of 1:1:2, add a combustion aid MnO 2 content of 0.18%, and a desulfurization and dechlorination agent CaO content of 0.90 %, mix evenly, and keep the moisture content at 8% to 12%; then knead and shape, and then dry naturally to a solid fuel product with a moisture content of 5% to 15%. The compressive strength of the solid fuel is measured by "Method for Determination of Cold Compressive Strength of Industrial Briquette" (MT/T748-1997), and the compressive strength of the solid fuel is determined to be in the range of 167.2620kPa to 207.0788kPa, with a reliability of 95%.
[实施例2][Example 2]
将烘干后水分含量为4%~8%的有机垃圾颗粒、煤粉颗粒、污泥按2∶1∶1比例混合,加入助燃剂MnO2含量为0.17%,脱硫脱氯剂CaO含量为1.20%,混合均匀,保持水分含量为8%~12%;然后混捏加工成型,再经自然干燥至水分含量为5%~15%的固体燃料产品。将成型固体燃料产品在水中(室温状态下)浸泡24h后,采用《工业型煤浸水强度和浸水复干强度的测定方法》(MT/T749-1997)测定该固体燃料的浸水强度,经测定该固体燃料的浸水强度在18.74458kPa~23.484038kPa范围,可靠性为95%。Mix organic waste particles, coal powder particles, and sludge with a moisture content of 4% to 8% after drying in a ratio of 2:1:1, add a combustion aid MnO 2 content of 0.17%, and a desulfurization and dechlorination agent CaO content of 1.20 %, mix evenly, and keep the moisture content at 8% to 12%; then knead and shape, and then dry naturally to a solid fuel product with a moisture content of 5% to 15%. After immersing the molded solid fuel product in water (at room temperature) for 24 hours, the water immersion strength of the solid fuel was measured using the "Measurement Method for Water Immersion Strength and Water Immersion Re-drying Strength of Industrial Briquettes" (MT/T749-1997). The water immersion strength of the solid fuel is in the range of 18.74458kPa to 23.484038kPa, and the reliability is 95%.
[实施例3][Example 3]
将烘干后水分含量为4%~8%的有机垃圾颗粒、煤粉颗粒、污泥按2∶1∶1比例混合,加入助燃剂MnO2含量为0.18%,脱硫脱氯剂CaO含量为1.20%,混合均匀,保持水分含量为8%~12%,然后混捏加工成型,再经自然干燥至水分含量为5%~15%的固体燃料产品。采用《工业型煤浸水强度和浸水复干强度的测定方法》(MT/T749-1997)测定该固体燃料的浸水复干强度,经测定该固体燃料的浸水复干强度在58.32095kPa~66.58751kPa范围,可靠性为95%。Mix organic waste particles, coal powder particles, and sludge with a moisture content of 4% to 8% after drying in a ratio of 2:1:1, add a combustion aid MnO 2 content of 0.18%, and a desulfurization and dechlorination agent CaO content of 1.20 %, mix evenly, keep the moisture content at 8% to 12%, then knead and shape, and then dry naturally to a solid fuel product with a moisture content of 5% to 15%. Using the "Measurement Method for Immersion Strength and Immersion Re-drying Strength of Industrial Briquettes" (MT/T749-1997) to measure the water-immersion and re-drying strength of the solid fuel, the water-immersion and re-drying strength of the solid fuel is determined to be in the range of 58.32095kPa~66.58751kPa , with a reliability of 95%.
[实施例4][Example 4]
将烘干后水分含量为4%~8%有机垃圾颗粒、煤粉颗粒、污泥按2∶1∶1比例混合,加入助燃剂MnO2含量为0.19%,脱硫脱氯剂CaO含量为0.90%,混合均匀,保持水分含量为8%~12%,然后混捏加工成型,再经自然干燥至水分含量为5%~15%的固体燃料产品。采用《煤的热稳定性测定方法》(GB/T 1573-2001)测定该固体燃料的热稳定性,经测定该固体燃料的热稳定性在69.895%~83.581%范围,可靠性为95%。After drying, the organic waste particles, coal powder particles, and sludge with a moisture content of 4% to 8% are mixed in a ratio of 2:1:1, and the content of MnO2 is 0.19%, and the content of desulfurization and dechlorination agent CaO is 0.90%. , mix evenly, keep the moisture content at 8% to 12%, then knead and shape, and then dry naturally to a solid fuel product with a moisture content of 5% to 15%. The thermal stability of the solid fuel was measured using the "Measurement Method for Thermal Stability of Coal" (GB/T 1573-2001), and the thermal stability of the solid fuel was determined to be in the range of 69.895% to 83.581%, with a reliability of 95%.
[实施例5][Example 5]
将烘干后水分含量为4%~8%的有机垃圾颗粒、污泥、煤粉颗粒按1∶1∶2比例混合,加入助燃剂MnO2含量为0.19%,脱硫脱氯剂CaO含量为1.20%,混合均匀,保持水分含量为8%~12%;然后混捏加工成型,再经自然干燥至水分含量为5%~15%的固体燃料产品。采用《煤的发热量测定方法》(GB/T213-1996)测定该固体燃料的燃烧热值,经测定该固体燃料的燃烧热值在18.92722~19.51157kJ/g范围,可靠性为95%。Mix organic waste particles, sludge, and coal powder particles with a moisture content of 4% to 8% after drying in a ratio of 1:1:2, add a combustion aid MnO 2 content of 0.19%, and a desulfurization and dechlorination agent CaO content of 1.20 %, mix evenly, and keep the moisture content at 8% to 12%; then knead and shape, and then dry naturally to a solid fuel product with a moisture content of 5% to 15%. The combustion calorific value of the solid fuel is measured by "Measurement Method for Calorific Value of Coal" (GB/T213-1996), and the calorific value of the solid fuel is determined to be in the range of 18.92722 to 19.51157 kJ/g, with a reliability of 95%.
[实施例6][Example 6]
将烘干后水分含量为4%~8%有机垃圾颗粒、煤粉颗粒、污泥按2∶1∶1比例混合,加入助燃剂MnO2含量为0.19%,脱硫脱氯剂CaO含量为1.50%,混合均匀,保持水分含量为8%~12%;然后混捏加工成型,再经自然干燥至水分含量为5%~15%的固体燃料产品。采用脱硫剂的固硫率(灰渣含硫量占固体燃料含硫量的百分率)指标衡量对污染气体的控制效果,即采用《煤中全硫的测定方法》(GB/T 214-1996)测定该固体燃料及灰渣的含硫量,经测定该固体燃料的固硫率在73.675%~91.461%范围,可靠性为95%。Mix organic waste particles, coal powder particles, and sludge with a moisture content of 4% to 8% after drying in a ratio of 2:1:1, add a combustion aid MnO 2 content of 0.19%, and a desulfurization and dechlorination agent CaO content of 1.50% , mix evenly, and keep the moisture content at 8% to 12%; then knead and shape, and then dry naturally to a solid fuel product with a moisture content of 5% to 15%. The sulfur fixation rate of the desulfurizer (the percentage of sulfur content in ash to the sulfur content of solid fuel) is used to measure the control effect on polluted gases, that is, the method for the determination of total sulfur in coal (GB/T 214-1996) The sulfur content of the solid fuel and ash is measured, and the sulfur fixation rate of the solid fuel is determined to be in the range of 73.675% to 91.461%, and the reliability is 95%.
[实施例7][Example 7]
将烘干后水分含量为4%~8%有机垃圾颗粒、煤粉颗粒、污泥按2∶1∶1比例混合,加入助燃剂MnO2含量为0.17%,脱硫脱氯剂CaO含量为0.80%,混合均匀,保持水分含量为8%~12%;然后混捏加工成型,再经自然干燥至水分含量为5%~15%的固体燃料产品。采用《煤中氯的测定方法》(GB 3558-1996)测定该固体燃料的脱氯率在57.761%~91.601%范围,可靠性为95%。Mix organic waste particles, coal powder particles, and sludge with a moisture content of 4% to 8% after drying in a ratio of 2:1:1, add a combustion aid MnO 2 content of 0.17%, and a desulfurization and dechlorination agent CaO content of 0.80% , mix evenly, and keep the moisture content at 8% to 12%; then knead and shape, and then dry naturally to a solid fuel product with a moisture content of 5% to 15%. The dechlorination rate of the solid fuel is measured in the range of 57.761% to 91.601% by "Determination of Chlorine in Coal" (GB 3558-1996), and the reliability is 95%.
[实施例8][Example 8]
将烘干后水分含量为4%~8%有机垃圾颗粒、煤粉颗粒、污泥按2∶1∶1比例混合,加入助燃剂MnO2含量为0.18%,脱硫脱氯剂CaO含量为1.50%,混合均匀,保持水分含量为8%~12%,然后混捏加工成型,再经自然干燥至水分含量为5%~15%的固体燃料产品。采用上述方法分别测定该固体燃料的抗压强度、浸水强度、浸水复干强度、热稳定性和燃烧热值,测定结果为:抗压强度达150.2891kPa,浸水强度达15.2634kPa,浸水复干强度达59.78425kPa,热稳定性指标TS+6值为62.98%,燃烧热值为18.27323kJ/g,固硫效率可达78.44%,固氯效率可达77.71%。Mix organic waste particles, coal powder particles, and sludge with a moisture content of 4% to 8% after drying in a ratio of 2:1:1, add a combustion aid MnO 2 content of 0.18%, and a desulfurization and dechlorination agent CaO content of 1.50% , mix evenly, keep the moisture content at 8% to 12%, then knead and shape, and then dry naturally to a solid fuel product with a moisture content of 5% to 15%. The compressive strength, water immersion strength, water immersion and re-drying strength, thermal stability and combustion calorific value of the solid fuel were respectively measured by the above method. It reaches 59.78425kPa, the thermal stability index TS +6 value is 62.98%, the combustion heat value is 18.27323kJ/g, the sulfur fixation efficiency can reach 78.44%, and the chlorine fixation efficiency can reach 77.71%.
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