CN103147434B - Treatment system and method for consolidating soft soil foundation by utilizing industrial waste gas heat - Google Patents
Treatment system and method for consolidating soft soil foundation by utilizing industrial waste gas heat Download PDFInfo
- Publication number
- CN103147434B CN103147434B CN201310122135.0A CN201310122135A CN103147434B CN 103147434 B CN103147434 B CN 103147434B CN 201310122135 A CN201310122135 A CN 201310122135A CN 103147434 B CN103147434 B CN 103147434B
- Authority
- CN
- China
- Prior art keywords
- waste gas
- control valve
- gas
- pipe
- chamber
- 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.)
- Active
Links
- 239000007789 gas Substances 0.000 title claims abstract description 160
- 239000002689 soil Substances 0.000 title claims abstract description 69
- 239000002440 industrial waste Substances 0.000 title claims abstract description 39
- 238000000034 method Methods 0.000 title claims abstract description 21
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 claims abstract description 134
- 238000000354 decomposition reaction Methods 0.000 claims abstract description 106
- 238000010521 absorption reaction Methods 0.000 claims abstract description 70
- 238000003756 stirring Methods 0.000 claims abstract description 68
- 239000001569 carbon dioxide Substances 0.000 claims abstract description 67
- 229910002092 carbon dioxide Inorganic materials 0.000 claims abstract description 67
- 239000002912 waste gas Substances 0.000 claims abstract description 49
- 238000000926 separation method Methods 0.000 claims abstract description 30
- 238000000746 purification Methods 0.000 claims abstract description 12
- 239000000203 mixture Substances 0.000 claims abstract description 10
- 239000000428 dust Substances 0.000 claims abstract description 9
- 238000005260 corrosion Methods 0.000 claims description 49
- 238000006243 chemical reaction Methods 0.000 claims description 32
- ODINCKMPIJJUCX-UHFFFAOYSA-N Calcium oxide Chemical compound [Ca]=O ODINCKMPIJJUCX-UHFFFAOYSA-N 0.000 claims description 24
- 238000009833 condensation Methods 0.000 claims description 21
- 230000005494 condensation Effects 0.000 claims description 21
- 238000001816 cooling Methods 0.000 claims description 21
- 238000010438 heat treatment Methods 0.000 claims description 20
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 claims description 15
- 239000000843 powder Substances 0.000 claims description 14
- 239000000292 calcium oxide Substances 0.000 claims description 12
- 235000012255 calcium oxide Nutrition 0.000 claims description 12
- CDBYLPFSWZWCQE-UHFFFAOYSA-L Sodium Carbonate Chemical compound [Na+].[Na+].[O-]C([O-])=O CDBYLPFSWZWCQE-UHFFFAOYSA-L 0.000 claims description 11
- 238000009413 insulation Methods 0.000 claims description 11
- 230000009471 action Effects 0.000 claims description 10
- 238000007789 sealing Methods 0.000 claims description 10
- 238000012546 transfer Methods 0.000 claims description 10
- BVKZGUZCCUSVTD-UHFFFAOYSA-M Bicarbonate Chemical compound OC([O-])=O BVKZGUZCCUSVTD-UHFFFAOYSA-M 0.000 claims description 8
- FYYHWMGAXLPEAU-UHFFFAOYSA-N Magnesium Chemical compound [Mg] FYYHWMGAXLPEAU-UHFFFAOYSA-N 0.000 claims description 7
- 230000005484 gravity Effects 0.000 claims description 7
- 229910000029 sodium carbonate Inorganic materials 0.000 claims description 6
- 239000011777 magnesium Substances 0.000 claims description 4
- 229910052749 magnesium Inorganic materials 0.000 claims description 4
- 239000000463 material Substances 0.000 claims description 4
- 230000003647 oxidation Effects 0.000 claims description 4
- 238000007254 oxidation reaction Methods 0.000 claims description 4
- KWYUFKZDYYNOTN-UHFFFAOYSA-M Potassium hydroxide Chemical compound [OH-].[K+] KWYUFKZDYYNOTN-UHFFFAOYSA-M 0.000 claims description 3
- 150000004649 carbonic acid derivatives Chemical class 0.000 claims description 2
- 239000007788 liquid Substances 0.000 claims description 2
- 238000000197 pyrolysis Methods 0.000 claims description 2
- 150000001875 compounds Chemical class 0.000 claims 12
- 239000000376 reactant Substances 0.000 claims 8
- 230000006835 compression Effects 0.000 claims 3
- 238000007906 compression Methods 0.000 claims 3
- 238000002156 mixing Methods 0.000 claims 3
- BWHMMNNQKKPAPP-UHFFFAOYSA-L potassium carbonate Chemical compound [K+].[K+].[O-]C([O-])=O BWHMMNNQKKPAPP-UHFFFAOYSA-L 0.000 claims 2
- 230000008676 import Effects 0.000 claims 1
- 229910000027 potassium carbonate Inorganic materials 0.000 claims 1
- 238000009938 salting Methods 0.000 claims 1
- 238000005979 thermal decomposition reaction Methods 0.000 claims 1
- 239000003795 chemical substances by application Substances 0.000 abstract description 36
- 230000002787 reinforcement Effects 0.000 abstract description 9
- 238000010276 construction Methods 0.000 abstract description 7
- 239000003513 alkali Substances 0.000 abstract description 6
- 238000005086 pumping Methods 0.000 abstract description 6
- BVKZGUZCCUSVTD-UHFFFAOYSA-L Carbonate Chemical compound [O-]C([O-])=O BVKZGUZCCUSVTD-UHFFFAOYSA-L 0.000 abstract description 3
- 238000006477 desulfuration reaction Methods 0.000 abstract description 3
- 230000023556 desulfurization Effects 0.000 abstract description 3
- 239000000284 extract Substances 0.000 abstract 1
- 239000000243 solution Substances 0.000 description 93
- UIIMBOGNXHQVGW-UHFFFAOYSA-M sodium bicarbonate Substances [Na+].OC([O-])=O UIIMBOGNXHQVGW-UHFFFAOYSA-M 0.000 description 38
- 239000004568 cement Substances 0.000 description 19
- CPLXHLVBOLITMK-UHFFFAOYSA-N Magnesium oxide Chemical class [Mg]=O CPLXHLVBOLITMK-UHFFFAOYSA-N 0.000 description 14
- 229910000030 sodium bicarbonate Inorganic materials 0.000 description 14
- 235000017557 sodium bicarbonate Nutrition 0.000 description 14
- AXZKOIWUVFPNLO-UHFFFAOYSA-N magnesium;oxygen(2-) Chemical class [O-2].[Mg+2] AXZKOIWUVFPNLO-UHFFFAOYSA-N 0.000 description 13
- 238000003860 storage Methods 0.000 description 12
- 239000000395 magnesium oxide Substances 0.000 description 11
- TYJJADVDDVDEDZ-UHFFFAOYSA-M potassium hydrogencarbonate Chemical compound [K+].OC([O-])=O TYJJADVDDVDEDZ-UHFFFAOYSA-M 0.000 description 11
- 230000007613 environmental effect Effects 0.000 description 10
- DGAQECJNVWCQMB-PUAWFVPOSA-M Ilexoside XXIX Chemical compound C[C@@H]1CC[C@@]2(CC[C@@]3(C(=CC[C@H]4[C@]3(CC[C@@H]5[C@@]4(CC[C@@H](C5(C)C)OS(=O)(=O)[O-])C)C)[C@@H]2[C@]1(C)O)C)C(=O)O[C@H]6[C@@H]([C@H]([C@@H]([C@H](O6)CO)O)O)O.[Na+] DGAQECJNVWCQMB-PUAWFVPOSA-M 0.000 description 8
- 238000004519 manufacturing process Methods 0.000 description 8
- 230000000694 effects Effects 0.000 description 7
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 7
- VTYYLEPIZMXCLO-UHFFFAOYSA-L Calcium carbonate Chemical group [Ca+2].[O-]C([O-])=O VTYYLEPIZMXCLO-UHFFFAOYSA-L 0.000 description 6
- 238000003763 carbonization Methods 0.000 description 6
- 239000012295 chemical reaction liquid Substances 0.000 description 6
- 238000004321 preservation Methods 0.000 description 6
- 239000011734 sodium Substances 0.000 description 6
- 229910052708 sodium Inorganic materials 0.000 description 6
- 239000011398 Portland cement Substances 0.000 description 5
- 238000005516 engineering process Methods 0.000 description 5
- ZLNQQNXFFQJAID-UHFFFAOYSA-L magnesium carbonate Chemical compound [Mg+2].[O-]C([O-])=O ZLNQQNXFFQJAID-UHFFFAOYSA-L 0.000 description 5
- 239000001095 magnesium carbonate Substances 0.000 description 5
- 229910000021 magnesium carbonate Inorganic materials 0.000 description 5
- 235000015497 potassium bicarbonate Nutrition 0.000 description 5
- 229910000028 potassium bicarbonate Inorganic materials 0.000 description 5
- 239000011736 potassium bicarbonate Substances 0.000 description 5
- 238000005728 strengthening Methods 0.000 description 5
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 4
- ZLMJMSJWJFRBEC-UHFFFAOYSA-N Potassium Chemical compound [K] ZLMJMSJWJFRBEC-UHFFFAOYSA-N 0.000 description 4
- 239000011259 mixed solution Substances 0.000 description 4
- 239000011591 potassium Substances 0.000 description 4
- 229910052700 potassium Inorganic materials 0.000 description 4
- 229940001593 sodium carbonate Drugs 0.000 description 4
- 238000009423 ventilation Methods 0.000 description 4
- 238000010792 warming Methods 0.000 description 4
- 235000019738 Limestone Nutrition 0.000 description 3
- MWUXSHHQAYIFBG-UHFFFAOYSA-N Nitric oxide Chemical compound O=[N] MWUXSHHQAYIFBG-UHFFFAOYSA-N 0.000 description 3
- 229910000019 calcium carbonate Inorganic materials 0.000 description 3
- 239000000378 calcium silicate Substances 0.000 description 3
- 229910052918 calcium silicate Inorganic materials 0.000 description 3
- OYACROKNLOSFPA-UHFFFAOYSA-N calcium;dioxido(oxo)silane Chemical compound [Ca+2].[O-][Si]([O-])=O OYACROKNLOSFPA-UHFFFAOYSA-N 0.000 description 3
- 229910052799 carbon Inorganic materials 0.000 description 3
- 230000006837 decompression Effects 0.000 description 3
- 239000006028 limestone Substances 0.000 description 3
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 2
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 description 2
- AXCZMVOFGPJBDE-UHFFFAOYSA-L calcium dihydroxide Chemical compound [OH-].[OH-].[Ca+2] AXCZMVOFGPJBDE-UHFFFAOYSA-L 0.000 description 2
- 239000000920 calcium hydroxide Substances 0.000 description 2
- 229910001861 calcium hydroxide Inorganic materials 0.000 description 2
- 229910002091 carbon monoxide Inorganic materials 0.000 description 2
- BVKZGUZCCUSVTD-UHFFFAOYSA-N carbonic acid Chemical compound OC(O)=O BVKZGUZCCUSVTD-UHFFFAOYSA-N 0.000 description 2
- 230000008859 change Effects 0.000 description 2
- 239000004020 conductor Substances 0.000 description 2
- 238000011161 development Methods 0.000 description 2
- 229910052757 nitrogen Inorganic materials 0.000 description 2
- 238000001556 precipitation Methods 0.000 description 2
- 230000008569 process Effects 0.000 description 2
- 230000009467 reduction Effects 0.000 description 2
- 238000011160 research Methods 0.000 description 2
- 239000002918 waste heat Substances 0.000 description 2
- 238000003466 welding Methods 0.000 description 2
- 229910021529 ammonia Inorganic materials 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000001354 calcination Methods 0.000 description 1
- 239000003245 coal Substances 0.000 description 1
- 238000002485 combustion reaction Methods 0.000 description 1
- 239000013078 crystal Substances 0.000 description 1
- 230000001186 cumulative effect Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- RCJVRSBWZCNNQT-UHFFFAOYSA-N dichloridooxygen Chemical compound ClOCl RCJVRSBWZCNNQT-UHFFFAOYSA-N 0.000 description 1
- 238000009826 distribution Methods 0.000 description 1
- TXKMVPPZCYKFAC-UHFFFAOYSA-N disulfur monoxide Inorganic materials O=S=S TXKMVPPZCYKFAC-UHFFFAOYSA-N 0.000 description 1
- 238000003912 environmental pollution Methods 0.000 description 1
- 239000000446 fuel Substances 0.000 description 1
- 238000001879 gelation Methods 0.000 description 1
- 239000005431 greenhouse gas Substances 0.000 description 1
- 238000006703 hydration reaction Methods 0.000 description 1
- VTHJTEIRLNZDEV-UHFFFAOYSA-L magnesium dihydroxide Chemical compound [OH-].[OH-].[Mg+2] VTHJTEIRLNZDEV-UHFFFAOYSA-L 0.000 description 1
- 239000000347 magnesium hydroxide Substances 0.000 description 1
- 229910001862 magnesium hydroxide Inorganic materials 0.000 description 1
- 238000010248 power generation Methods 0.000 description 1
- 238000012545 processing Methods 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 238000004064 recycling Methods 0.000 description 1
- 230000003014 reinforcing effect Effects 0.000 description 1
- 239000004054 semiconductor nanocrystal Substances 0.000 description 1
- 238000007711 solidification Methods 0.000 description 1
- 230000008023 solidification Effects 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- XTQHKBHJIVJGKJ-UHFFFAOYSA-N sulfur monoxide Chemical compound S=O XTQHKBHJIVJGKJ-UHFFFAOYSA-N 0.000 description 1
- 238000012360 testing method Methods 0.000 description 1
Landscapes
- Gas Separation By Absorption (AREA)
- Treating Waste Gases (AREA)
Abstract
本发明提供了一种利用工业废气热加固软土地基的处理系统及方法,该处理系统包括工业废气热分离装置、废气净化装置、尾气收集处理装置、地基土搅拌装置、气体泵入装置。处理系统采用经除尘、脱硫、脱硝后的废气热,经分离装置和净化装置提取纯净二氧化碳,用搅拌装置将固化剂拌入地基土中,利用气体泵入装置将纯净二氧化碳泵入混合土中来碳化加固软土地基。废气净化装置包括吸收室和分解室,均是带阀门的密闭装置,装置内的净化溶液为碱溶液或碳酸盐溶液,或其混合液,可循环利用。该方法和处理系统充分利用工业的废气热,解决了工业废气热资源化利用的难题,同时提高了地基加固的施工效率和地基土强度。
The invention provides a treatment system and method for using industrial waste gas heat to strengthen soft ground. The treatment system includes an industrial waste gas thermal separation device, a waste gas purification device, a tail gas collection and treatment device, a foundation soil stirring device, and a gas pumping device. The treatment system uses the waste gas heat after dust removal, desulfurization and denitrification, extracts pure carbon dioxide through the separation device and purification device, mixes the curing agent into the foundation soil with the stirring device, and pumps the pure carbon dioxide into the mixed soil with the gas pumping device. Carbonation strengthens soft ground. The exhaust gas purification device includes an absorption chamber and a decomposition chamber, both of which are closed devices with valves. The purification solution in the device is alkali solution or carbonate solution, or a mixture thereof, which can be recycled. The method and treatment system make full use of industrial waste gas heat, solve the problem of resource utilization of industrial waste gas heat, and simultaneously improve the construction efficiency of foundation reinforcement and the strength of foundation soil.
Description
技术领域technical field
本发明涉及一种加固软土地基的处理系统及方法,特别涉及一种利用工业废气热加固软土地基的处理系统及方法,属于环境岩土工程技术领域。The invention relates to a treatment system and method for strengthening soft soil foundations, in particular to a treatment system and method for strengthening soft soil foundations by using industrial waste gas heat, and belongs to the technical field of environmental geotechnical engineering.
背景技术Background technique
2007年,政府间气候变化专门委员会(IPCC)第四次评估报告中指出:“自20世纪中期以来全球气候变暖是由于人为温室气体的排放增加所致,尤其是二氧化碳”。目前,人类活动引起全球二氧化碳的排放量约为每年240亿吨,累计的二氧化碳浓度为379ppm,超过工业化前的33%,并且每年将以超过1ppm的速度增加,给全球造成了许多重大灾难。据文献统计,二氧化碳的排放量到2025年将增加到388亿吨,全世界环境难民已达2500万人,预计到2050年,全球变暖导致的环境难民将达到1.5亿人,中国也深受气候变暖的危害。据2008年的《中国应对气候变化的政策与行动》白皮书所述,中国气候变暖的趋势与全球的总趋势基本一致。中国百年来(1908-2007年)地表平均气温升高了1.1℃,近30年来,中国沿海的海表面温度上升了0.9℃,沿海海平面上升了9cm。中国科学家的预测结果表明:2020年中国年平均气温将升高1.3℃~2.1℃,2050年将升高2.3℃~3.3℃。这将引起极端天气气候事件发生频率增加,降水分布不均现象更加明显,强降水事件发生频率增加,干旱范围继续扩大,海平面上升趋势进一步加剧。因此,二氧化碳减排已成为制约经济社会和生态环境发展的瓶颈。In 2007, the Fourth Assessment Report of the Intergovernmental Panel on Climate Change (IPCC) pointed out: "Global climate warming since the middle of the 20th century is due to the increase in man-made greenhouse gas emissions, especially carbon dioxide." At present, the global carbon dioxide emissions caused by human activities are about 24 billion tons per year, and the cumulative carbon dioxide concentration is 379ppm, which is 33% higher than that before industrialization, and will increase at a rate of more than 1ppm every year, causing many major disasters to the world. According to literature statistics, carbon dioxide emissions will increase to 38.8 billion tons by 2025, and the number of environmental refugees in the world has reached 25 million. It is estimated that by 2050, the number of environmental refugees caused by global warming will reach 150 million. China is also deeply affected The dangers of climate warming. According to the 2008 white paper "China's Policies and Actions to Address Climate Change", the trend of climate warming in China is basically consistent with the general trend of the world. Over the past 100 years (1908-2007), the average surface temperature in China has increased by 1.1°C. In the past 30 years, the sea surface temperature along China's coast has risen by 0.9°C, and the coastal sea level has risen by 9cm. The prediction results of Chinese scientists show that the average annual temperature in China will rise by 1.3°C to 2.1°C in 2020, and by 2.3°C to 3.3°C in 2050. This will lead to an increase in the frequency of extreme weather and climate events, more pronounced uneven distribution of precipitation, an increase in the frequency of heavy precipitation events, continued expansion of droughts, and further intensification of sea level rise. Therefore, carbon dioxide emission reduction has become a bottleneck restricting the development of economic society and ecological environment.
水泥生产排放的二氧化碳包括:煅烧熟料和燃料直接产生的二氧化碳和煅烧石灰石间接生成的二氧化碳;理论上,每生产1吨水泥熟料生成0.511吨二氧化碳,煤燃烧产生0.383~0.704吨二氧化碳。加上生成熟料时碳酸钙分解产生的二氧化碳,每生产1吨水泥熟料排放0.894~1.215吨二氧化碳,一般来说,每生产1吨水泥熟料排放约1吨二氧化碳。目前,每年全球波兰特水泥的产量超过25亿吨,并且预计到2050年可翻一倍,水泥生产产生的二氧化碳相当于所有全球人为排放的5~10%,有统计称,我国2008年水泥量超过7亿吨,水泥生产过程中的二氧化碳排放总量约占全国二氧化碳排放总量的18%~22%。The carbon dioxide emitted by cement production includes: carbon dioxide directly produced by calcined clinker and fuel and indirectly produced by calcined limestone; theoretically, every ton of cement clinker produced produces 0.511 tons of carbon dioxide, and coal combustion produces 0.383-0.704 tons of carbon dioxide. Adding the carbon dioxide produced by the decomposition of calcium carbonate during clinker production, 0.894-1.215 tons of carbon dioxide is emitted for every ton of cement clinker produced. Generally speaking, about 1 ton of carbon dioxide is emitted for every ton of cement clinker produced. At present, the annual output of Portland cement in the world exceeds 2.5 billion tons, and it is expected to double by 2050. The carbon dioxide produced by cement production is equivalent to 5-10% of all global man-made emissions. According to statistics, my country's cement production in 2008 More than 700 million tons, the total carbon dioxide emissions in the cement production process account for about 18% to 22% of the country's total carbon dioxide emissions.
中国作为负责任的发展中大国和京都协定的签约国,承担着很重的二氧化碳减排责任,二氧化碳的减排、捕捉和封存已引起政府和科研界的关注,是当前环境工程研究的一个重点问题。但二氧化碳捕捉和封存技术仍处于探索和初始阶段,其安全性有待继续检验,成本相对较高。然而工程建设中水泥生产是二氧化碳产生的重要来源之一,国内外科学家早已开始研究波兰特水泥的替代品,如1867年法国所瑞尔(Sorel)发明的Sorel水泥,也称镁水泥或氯氧镁水泥;澳大利亚科学家John Harrison在2001和2004年利用活性氧化镁发明了Tec-cements、Eco-cements和Enviro-cements三种“绿色水泥”。同时Harrison强调了新型含镁水泥具有一些优于波兰特水泥的优势,如活性氧化镁可在比波兰特水泥低600~750℃的温度下生产,而水泥生产的煅烧温度高达1450℃;生产1吨氧化镁需要2.08吨的碳酸镁,产生约1.4吨的二氧化碳排放,生产1吨生石灰则需要1.8吨石灰石,并且排放约0.79吨二氧化碳;此外,生石灰是早期主要的土体固化剂,生石灰与土中的水分快速发生水化反应并生成氢氧化钙,该反应会降低土体中的含水量,改善土体性质,氢氧化钙经胶凝作用生成了硅酸钙,若通入二氧化碳也可由部分石灰石生成,从而提高固化土的强度。活性氧化镁在常温下可与水迅速发生反应,生成氢氧化镁,在通入二氧化碳作用下,可在数小时内完成碳化,能提高固化土的强度,经测试其强度并不低于水泥土的强度,同时吸收了二氧化碳,具有显著的环境效应。As a responsible developing country and a signatory to the Kyoto Agreement, China bears a heavy responsibility for reducing carbon dioxide emissions. The reduction, capture and storage of carbon dioxide has attracted the attention of the government and the scientific research community, and is a focus of current environmental engineering research. question. However, the carbon dioxide capture and storage technology is still in the exploration and initial stage, its safety needs to be further tested, and the cost is relatively high. However, cement production in engineering construction is one of the important sources of carbon dioxide. Scientists at home and abroad have already begun to study substitutes for Portland cement, such as Sorel cement invented by Sorel in France in 1867, also known as magnesium cement or oxychloride. Magnesium cement; Australian scientist John Harrison invented three "green cements" in 2001 and 2004 using activated magnesia: Tec-cements, Eco-cements and Enviro-cements. At the same time, Harrison emphasized that the new magnesium-containing cement has some advantages over Portland cement. For example, activated magnesium oxide can be produced at a temperature 600-750°C lower than Portland cement, while the calcination temperature for cement production is as high as 1450°C; One ton of magnesium oxide requires 2.08 tons of magnesium carbonate, which produces about 1.4 tons of carbon dioxide emissions. The production of one ton of quicklime requires 1.8 tons of limestone and emits about 0.79 tons of carbon dioxide. In addition, quicklime is the main soil curing agent in the early stage. The water in the water quickly undergoes hydration reaction and generates calcium hydroxide. This reaction will reduce the water content in the soil and improve the properties of the soil. Calcium hydroxide will form calcium silicate through gelation. If carbon dioxide is introduced, it can also be partly Limestone is formed, which increases the strength of the solidified soil. Activated magnesium oxide can quickly react with water at room temperature to form magnesium hydroxide, which can be carbonized within a few hours under the action of carbon dioxide, which can improve the strength of solidified soil, and its strength is not lower than that of cement soil after testing The strength, while absorbing carbon dioxide, has a significant environmental effect.
我国处于工程建设的快速发展时期,仍有大量的地基加固工程,并且我国已有很多关于地基加固的技术和方法,但是目前所具有的处理装置在满足低碳环保和施工效率等方面仍存很大差距。my country is in a period of rapid development of engineering construction, there are still a large number of foundation reinforcement projects, and there are many technologies and methods for foundation reinforcement in my country, but the current processing devices still have a lot of problems in terms of meeting low-carbon environmental protection and construction efficiency. big gap.
因此,结合以上环境问题和我国目前的现状,开发和研制一种具有自主知识产权的利用工业废气热加固软土地基的处理系统和方法,对我国二氧化碳减排、改善生态环境和提高地基加固效率等方面具有重要意义。Therefore, combining the above environmental problems and the current status quo of our country, develop and develop a treatment system and method with independent intellectual property rights for the use of industrial waste gas heat reinforcement of soft soil foundation, which will reduce carbon dioxide emissions, improve the ecological environment and improve the efficiency of foundation reinforcement in my country. etc. are of great significance.
发明内容Contents of the invention
针对上述存在的环境问题和工业废气热的可利用性,本发明的目的在于提供一种低碳、环保利用工业废气热加固软土地基的处理系统及方法,同时该发明也可提高地基的加固效率。In view of the above-mentioned environmental problems and the availability of industrial waste heat, the purpose of the present invention is to provide a low-carbon, environmentally friendly treatment system and method for strengthening soft soil foundations by using industrial waste heat. At the same time, the invention can also improve the reinforcement of the foundation. efficiency.
其技术解决方案为:Its technical solutions are:
一种利用工业废气热加固软土地基的处理系统,其特征在于:包括废气热分离装置5、废气净化装置、尾气收集处理装置15、地基土搅拌装置、气体泵入装置,所述废气热分离装置5的进气口与防腐保温管4的后端密封连接,防腐保温管4的前端与烟囱1的排气口顶端通过法兰盘2密封连接,防腐保温管4上设有排气阀A3,所述废气净化装置包括吸收室8和分解室10,吸收室8底部与废气热分离装置5通过防腐导气管6连接,防腐导气管6的一端与废气热分离装置5相连接,防腐导气管6的另一端伸入到吸收室8内底部,吸收室8的底部与分解室10的底部通过冷凝管19连通,冷凝管19上装有冷凝器18,吸收室8和冷凝器18之间的冷凝管上设有控制阀B17,分解室10置于加热箱9中,废气热分离装置5与加热箱9通过防腐导热管7连接,防腐导热管7一端与废气热分离装置5连接,防腐导热管7的另一端伸入到加热箱9中,尾气收集处理装置15与吸收室8顶端通过防腐导气管14连接,防腐导气管14上设有控制阀A13,分解室10内设有温度传感器40,吸收室8顶端上设有降压排气管11,降压排气管11上设有排气阀B12,所述搅拌装置包括桩机架29、搅拌轴32、多个搅拌叶片33、固化剂储藏容器31和固化剂输送管30,搅拌轴32竖直附着在桩机架29上,搅拌轴32与固化剂储藏容器31通过固化剂输送管30连接,所述多个搅拌叶片33固定在搅拌轴32上,所述气体泵入装置包括减压阀20、冷却抽气泵21、气体流量计22、导气管23、控制阀C24、高压气瓶25、压力泵26、高压管36和压力控制阀37,分解室10顶端与高压气瓶25顶端通过导气管23密封连接,从分解室10到高压气瓶25的方向上,导气管23上依次设有减压阀20、冷却抽气泵21、气体流量计22和控制阀C24,其中减压阀20置于分解室10顶端和冷却抽气泵21之间,与分解室10顶端和冷却抽气泵21相邻,冷却抽气泵21置于减压阀20和气体流量计22之间,与减压阀20和气体流量计22相邻,控制阀C24置于气体流量计22和高压气瓶25顶端之间,与气体流量计22和高压气瓶25顶端相邻,压力泵26置于高压气瓶25顶端,多个导入管27插入地基土28中,所述多个导入管27分别与支管38连接,高压管36的一端与高压气瓶25的内顶端连通,另一端通过压力控制阀37与支管38连接。A treatment system for using industrial waste gas heat to strengthen soft ground, characterized in that it includes a waste gas thermal separation device 5, a waste gas purification device, a tail gas collection and treatment device 15, a foundation soil stirring device, and a gas pumping device. The air inlet of the device 5 is sealed and connected to the rear end of the anti-corrosion heat preservation pipe 4, the front end of the anti-corrosion heat preservation pipe 4 is sealed and connected to the top of the exhaust port of the chimney 1 through the flange plate 2, and the anti-corrosion heat preservation pipe 4 is provided with an exhaust valve A3 , the waste gas purification device includes an absorption chamber 8 and a decomposition chamber 10, the bottom of the absorption chamber 8 is connected with the waste gas heat separation device 5 through an anti-corrosion air guide pipe 6, and one end of the anti-corrosion air guide pipe 6 is connected with the waste gas heat separation device 5, and the anti-corrosion air guide pipe The other end of 6 stretches into the inner bottom of absorption chamber 8, and the bottom of absorption chamber 8 communicates with the bottom of decomposition chamber 10 through condensation pipe 19, and condenser 18 is housed on the condensation pipe 19, and the condensation between absorption chamber 8 and condenser 18 There is a control valve B17 on the pipe, the decomposition chamber 10 is placed in the heating box 9, the waste gas thermal separation device 5 is connected to the heating box 9 through the anti-corrosion heat transfer tube 7, and one end of the anti-corrosion heat transfer tube 7 is connected to the exhaust gas thermal separation device 5, and the anti-corrosion heat transfer tube The other end of 7 extends into the heating box 9, and the tail gas collection and treatment device 15 is connected to the top of the absorption chamber 8 through an anti-corrosion air guide tube 14. The anti-corrosion air guide tube 14 is provided with a control valve A13, and the decomposition chamber 10 is provided with a temperature sensor 40. The top of the absorption chamber 8 is provided with a step-down exhaust pipe 11, and the step-down exhaust pipe 11 is provided with an exhaust valve B12. Storage container 31 and curing agent delivery pipe 30, stirring shaft 32 is vertically attached on the pile frame 29, and stirring shaft 32 is connected with curing agent storage container 31 by curing agent delivery pipe 30, and described a plurality of stirring blades 33 are fixed on stirring On the shaft 32, the gas pumping device includes a pressure reducing valve 20, a cooling air pump 21, a gas flow meter 22, an air guide pipe 23, a control valve C24, a high-pressure gas cylinder 25, a pressure pump 26, a high-pressure pipe 36 and a pressure control valve 37. The top of the decomposition chamber 10 and the top of the high-pressure gas cylinder 25 are sealed and connected through the air guide tube 23. In the direction from the decomposition chamber 10 to the high-pressure gas cylinder 25, the air guide tube 23 is sequentially provided with a pressure reducing valve 20, a cooling air pump 21, a gas Flowmeter 22 and control valve C24, wherein the pressure reducing valve 20 is placed between the top of the decomposition chamber 10 and the cooling air pump 21, adjacent to the top of the decomposition chamber 10 and the cooling air pump 21, and the cooling air pump 21 is placed on the pressure reducing valve 20 Between the gas flow meter 22 and adjacent to the pressure reducing valve 20 and the gas flow meter 22, the control valve C24 is placed between the gas flow meter 22 and the top of the high-pressure gas cylinder 25, and connected to the top of the gas flow meter 22 and the high-pressure gas cylinder 25 Adjacent, the pressure pump 26 is placed on the top of the high-pressure gas cylinder 25, and a plurality of introduction pipes 27 are inserted into the foundation soil 28. The top end communicates, and the other end is connected with the branch pipe 38 through the pressure control valve 37 .
进一步地,吸收室8、分解室10和加热箱9均为密封容器,吸收室8中盛放反应液16,分解室10底部高度不低于吸收室8中反应液16的上平面,吸收室8采用防腐材料制作,分解室10采用防腐且导热的材料制作。Further, the absorption chamber 8, the decomposition chamber 10 and the heating box 9 are all sealed containers, the absorption chamber 8 contains the reaction solution 16, and the height of the bottom of the decomposition chamber 10 is not lower than the upper plane of the reaction solution 16 in the absorption chamber 8, and the absorption chamber 8 is made of anti-corrosion material, and the decomposition chamber 10 is made of anti-corrosion and heat-conducting material.
进一步地,所述多个搅拌叶片33通过螺栓或焊接连接在搅拌轴32的低端,搅拌轴32为中空状的,所述多个搅拌叶片33为对称排布,可为2或3层,在搅拌轴低端的两层搅拌叶片33之间的搅拌轴32上设有固化剂喷口34。Further, the plurality of stirring blades 33 are connected to the lower end of the stirring shaft 32 by bolts or welding, the stirring shaft 32 is hollow, and the plurality of stirring blades 33 are symmetrically arranged and may be 2 or 3 layers, A curing agent spout 34 is provided on the stirring shaft 32 between the two layers of stirring blades 33 at the lower end of the stirring shaft.
进一步地,导入管27上设有双排通气孔39,导入管27与支管38相连,支管38上方的地基土28表面覆设有密封膜35。Further, the introduction pipe 27 is provided with double rows of ventilation holes 39 , the introduction pipe 27 is connected to the branch pipe 38 , and the surface of the foundation soil 28 above the branch pipe 38 is covered with a sealing film 35 .
一种利用工业废气热加固软土地基的方法,其特征在于采用以下步骤实现:A method for thermally reinforcing soft soil foundations by using industrial waste gas, characterized in that the following steps are adopted:
a.利用防腐保温管4将除尘、脱硫、脱硝后的工业废气热输入到废气热分离装置5中,分离后的废气通过防腐导气管6通入吸收室8中,分离后的热量通过防腐导热管7导入加热箱9中,a. Use the anti-corrosion insulation pipe 4 to input the heat of industrial waste gas after dust removal, desulfurization and denitrification into the waste gas heat separation device 5, and the separated waste gas is passed into the absorption chamber 8 through the anti-corrosion air guide tube 6, and the separated heat is conducted through the anti-corrosion heat conduction The tube 7 leads into the heating box 9,
b.在吸收室8中加入反应液16,关闭排气阀B12,打开控制阀A13,分离后的废气与反应液16充分反应后,关闭控制阀A13和减压阀20,打开控制阀B17和控制阀C24,废气将吸收室8中的反应后的溶液通过冷凝管19压入分解室10中,溶液完全进入分解室10后,关闭控制阀B17,打开控制阀A13,b. Add the reaction liquid 16 in the absorption chamber 8, close the exhaust valve B12, open the control valve A13, after the exhaust gas after separation fully reacts with the reaction liquid 16, close the control valve A13 and the pressure reducing valve 20, open the control valve B17 and Control valve C24, the exhaust gas presses the reacted solution in the absorption chamber 8 into the decomposition chamber 10 through the condensation pipe 19, after the solution completely enters the decomposition chamber 10, close the control valve B17, open the control valve A13,
c.分解室10中的溶液在热解作用下分解,生成二氧化碳气体和水蒸气,关闭压力控制阀37,冷却抽气泵21除去生成气体中的水蒸气,并将二氧化碳气体通过导气管23通入高压气瓶25中,c. The solution in the decomposition chamber 10 decomposes under pyrolysis, generates carbon dioxide gas and water vapor, closes the pressure control valve 37, cools the air pump 21 and removes the water vapor in the generated gas, and passes the carbon dioxide gas through the air guide tube 23 High-pressure cylinder 25,
d.气体流量计22测量的当前流量低于正常流量的10%时,关闭控制阀C24,打开控制阀B17和控制阀A13和减压阀20,分解室10中的溶液在重力作用下经冷凝管19和冷凝器18流入吸收室8中,然后关闭控制阀B17,d. when the current flow measured by the gas flow meter 22 is lower than 10% of the normal flow, close the control valve C24, open the control valve B17, the control valve A13 and the pressure reducing valve 20, and the solution in the decomposition chamber 10 is condensed under the action of gravity Pipe 19 and condenser 18 flow into the absorption chamber 8, then close the control valve B17,
e.重复实施步骤a-d,不断产生气体,e. Repeat steps a-d to continuously generate gas,
f.根据搅拌叶片33的半径和搅拌轴32的提升速度和旋转速度,设置固化剂输送率,通过地基土搅拌装置中的固化剂输送管30、搅拌轴32和固化剂喷口34将固化剂从固化剂储藏容器31喷入在地基土28中,并通过搅拌叶片33将固化剂和地基土28均匀搅拌,f. according to the lifting speed and the rotation speed of the radius of stirring blade 33 and stirring shaft 32, setting curing agent delivery rate, by curing agent delivery pipe 30, stirring shaft 32 and curing agent spout 34 in foundation soil stirring device, curing agent is transferred from The curing agent storage container 31 is sprayed into the foundation soil 28, and the curing agent and the foundation soil 28 are uniformly stirred by the stirring blade 33,
g.打开压力控制阀37和压力泵26,将高压气瓶25中的气体通过高压管36、支管38、导入管27和通气孔39导入到地基土28中。g. Open the pressure control valve 37 and the pressure pump 26, and introduce the gas in the high-pressure cylinder 25 into the foundation soil 28 through the high-pressure pipe 36, the branch pipe 38, the introduction pipe 27 and the ventilation hole 39.
进一步地,所述分离后的废气包括二氧化碳气体,所述反应液16为碱溶液或饱和碳酸盐溶液。Further, the separated exhaust gas includes carbon dioxide gas, and the reaction solution 16 is an alkali solution or a saturated carbonate solution.
进一步地,所述的固化剂为活性氧化镁粉末、生石灰粉末或两者的混合物。Further, the curing agent is active magnesium oxide powder, quicklime powder or a mixture of both.
进一步地,所述反应液16为氢氧化钠溶液、氢氧化钾溶液、碳酸钠溶液、碳酸钾溶液或上述溶液的混合物,反应液16在吸收室8中反应后生成碳酸氢盐溶液,并被分离后的废气压入到分解室10中。Further, the reaction solution 16 is sodium hydroxide solution, potassium hydroxide solution, sodium carbonate solution, potassium carbonate solution or a mixture of the above solutions, and the reaction solution 16 generates bicarbonate solution after reacting in the absorption chamber 8, and is absorbed The separated waste gas is fed into the decomposition chamber 10 .
进一步地,所述分解室10中的温度传感器40所显示的分解室10的环境温度不低于反应液16反应以后且被压到分解室(10)中的碳酸氢盐热溶液分解的最低温度。Further, the ambient temperature of the decomposition chamber 10 shown by the temperature sensor 40 in the decomposition chamber 10 is not lower than the minimum temperature of the decomposition of the bicarbonate thermal solution that is pressed into the decomposition chamber (10) after the reaction solution 16 reacts .
本发明的有益效果是:The beneficial effects of the present invention are:
由于采用了以上技术方案,本发明的一种利用工业废气热加固软土地基的处理系统及方法,采用的二氧化碳为来自电厂、化工厂或水泥厂等经处理净化后的废气,减少了环境中二氧化碳的排放量,由于在净化废气中使用了钠、钾的碱溶液或钠、钾碳酸盐溶液或其混合液,在分解过程中也充分利用了工业中排放出的余热,同时也实现了钠、钾的碱溶液或钠、钾碳酸盐溶液或其混合液的循环利用,节约了废气净化的成本,保证了余热的充分利用;地基加固使用了活性氧化镁粉末、生石灰粉末或两者混合物,相比于普通波兰特水泥,生产相同质量的活性氧化镁和生石灰所排放的二氧化碳相对较少,在原料上也具有显著的低碳环保效应;将二氧化碳通入地基土中,在地基土的上表面铺盖了密封膜,在施工加固过程中也减少了二氧化碳的泄漏,所以在施工阶段也具有明显的环境效应;地基土采用以活性氧化镁和生石灰或两者混合物为固化剂,然后通入一定压力的二氧化碳,加速了地基土的碳化固化,实现了地基土强度的快速增长,具有较高的施工加固效率。Due to the adoption of the above technical scheme, a treatment system and method for thermally strengthening soft soil foundations using industrial waste gas of the present invention, the carbon dioxide used is the treated and purified waste gas from power plants, chemical plants or cement plants, etc., which reduces environmental pollution. The emission of carbon dioxide, due to the use of sodium, potassium alkali solution or sodium, potassium carbonate solution or their mixture in the purification of waste gas, also fully utilizes the waste heat discharged from the industry in the decomposition process, and also realizes The recycling of sodium and potassium alkali solution or sodium and potassium carbonate solution or their mixed solution saves the cost of exhaust gas purification and ensures the full utilization of waste heat; ground reinforcement uses activated magnesia powder, quicklime powder or both The mixture, compared with ordinary Portland cement, produces the same quality of activated magnesia and quicklime, which emits relatively less carbon dioxide, and also has a significant low-carbon environmental protection effect on raw materials; the carbon dioxide is passed into the foundation soil, and the foundation soil The upper surface of the upper surface is covered with a sealing film, which also reduces the leakage of carbon dioxide during the construction reinforcement process, so it also has obvious environmental effects during the construction stage; Injecting a certain pressure of carbon dioxide accelerates the carbonization and solidification of the foundation soil, realizes the rapid growth of the strength of the foundation soil, and has a high construction reinforcement efficiency.
附图说明Description of drawings
以下将结合附图1对本发明所述的利用工业废气热加固软土地基的处理系统及方法进行详细说明。The treatment system and method for thermally strengthening soft ground by using industrial waste gas according to the present invention will be described in detail below in conjunction with accompanying drawing 1 .
附图1是本发明的一种利用工业废气热加固软土地基的处理系统的示意图。Accompanying drawing 1 is a kind of schematic diagram of the treatment system of the present invention that utilizes industrial waste gas heat to strengthen soft ground.
其中:1-烟囱,2-法兰盘,3-排气阀A,4-防腐保温管,5-废气热分离装置,6-防腐导气管,7-防腐导热管,8-吸收室,9-加热箱,10-分解室,11-降压排气管,12-排气阀B,13-控制阀A,14-防腐导气管,15-尾气收集处理装置,16-反应液,17-控制阀B,18-冷凝器,19-冷凝管,20-减压阀,21-冷却抽气泵,22-气体流量计,23-导气管,24-控制阀C,25-高压气瓶,26-压力泵,27-导入管,28-地基土,29-桩机架,30-固化剂输送管,31-固化剂储藏容器,32-搅拌轴,33-搅拌叶片,34-固化剂喷口,35-密封膜,36-高压管,37-压力控制阀,38-支管,39-通气孔,40-温度传感器。Among them: 1-chimney, 2-flange, 3-exhaust valve A, 4-corrosion insulation pipe, 5-exhaust gas thermal separation device, 6-corrosion air guide tube, 7-corrosion heat conduction tube, 8-absorption chamber, 9 -Heating box, 10-Decomposition chamber, 11-Decompression exhaust pipe, 12-Exhaust valve B, 13-Control valve A, 14-Anti-corrosion air duct, 15-Tail gas collection and treatment device, 16-Reaction liquid, 17- Control valve B, 18-condenser, 19-condenser pipe, 20-pressure reducing valve, 21-cooling pump, 22-gas flow meter, 23-air guide pipe, 24-control valve C, 25-high pressure cylinder, 26 -pressure pump, 27-introduction pipe, 28-foundation soil, 29-pile frame, 30-curing agent delivery pipe, 31-curing agent storage container, 32-stirring shaft, 33-stirring blade, 34-curing agent spout, 35-sealing film, 36-high pressure pipe, 37-pressure control valve, 38-branch pipe, 39-air vent, 40-temperature sensor.
具体实施方式Detailed ways
一种利用工业废气热加固软土地基的处理系统及方法,处理系统主要由工业废气热分离装置5、废气净化装置、尾气收集处理装置15、地基土搅拌装置、气体泵入装置等组成,工业中直接产生的废气为二氧化碳、氮氧化物、硫氧化物、氮气、氨气、一氧化碳等,进入到过废气热分离装置5中的高温气体为除尘、脱硫、脱硝的气体,主要为一氧化碳、二氧化碳、氮气等。废气热分离装置5是一种吸收热量的装置,但并不吸收气体,经过废气热分离装置5的气体温度因热量被大部分吸收将会降低。其技术原理之一:类同于暖气片和太阳能吸热板,不过,常规的暖气片是内用的是以水为热媒介(最高温度可达98℃)或以蒸汽为热媒介(最高温度可达160℃),在此废气热分离装置5中可以导热油为热媒介(最高温度可达400℃)。其技术原理之二:可使用麻省理工学院(MIT)的马丁·马尔多瓦(Martin Maldovan)所研发的合金化半导体纳米晶体技术,“热声子(heatphonons)晶体”便可以控制热量的通路,将热能汇聚(通常用于热能发电),借助与该技术,废气热分离装置5也可大大吸收工业废气热中的热量。由于该技术在能源领域相对有较多研究,故在此仅作以简单说明。废气热分离装置5的进气口与防腐保温管4的后端密封连接,防腐保温管4前端与烟囱1排气口顶端通过法兰盘2密封连接,防腐保温管4上设有排气阀A3,废气净化装置由吸收室8和分解室10组成,吸收室8中盛放反应液16,反应液16主要为钠、钾的碱溶液或钠、钾的碳酸盐溶液或该碱溶液与碳酸盐溶液的混合液,与二氧化碳反应后生成钠或钾的碳酸氢盐溶液,分解室10中为吸收室8中经反应后的相应碳酸氢盐溶液,吸收室8反应完后在气压作用下压入分解室10中,分解室10中溶液热解后在自重作用下进入吸收室8中。装置设置中,确保分解室10底部的高度高于吸收室8中的上液面。A treatment system and method for using industrial waste gas heat to strengthen soft ground. The treatment system is mainly composed of an industrial waste gas heat separation device 5, a waste gas purification device, a tail gas collection and treatment device 15, a foundation soil stirring device, and a gas pumping device. The exhaust gas directly produced in the waste gas is carbon dioxide, nitrogen oxide, sulfur oxide, nitrogen, ammonia, carbon monoxide, etc., and the high-temperature gas that enters the waste gas thermal separation device 5 is dust removal, desulfurization, and denitrification gas, mainly carbon monoxide and carbon dioxide. , nitrogen, etc. The exhaust gas thermal separation device 5 is a device that absorbs heat, but does not absorb gas. The temperature of the gas passing through the exhaust gas thermal separation device 5 will decrease due to most of the heat being absorbed. One of its technical principles: similar to radiators and solar heat absorbing panels, however, conventional radiators use water as the heat medium (the highest temperature can reach 98°C) or steam as the heat medium (the highest temperature up to 160° C.), heat transfer oil can be used as the heat medium in the waste gas thermal separation device 5 (the maximum temperature can reach 400° C.). The second technical principle: using the alloyed semiconductor nanocrystal technology developed by Martin Maldovan of the Massachusetts Institute of Technology (MIT), "thermal phonons (heatphonons) crystals" can control the passage of heat , to gather heat energy (usually used for thermal power generation), with the help of this technology, the waste gas heat separation device 5 can also greatly absorb the heat in the heat of industrial waste gas. Since there are relatively many studies on this technology in the field of energy, it is only briefly described here. The air inlet of the waste gas thermal separation device 5 is sealed and connected with the rear end of the anti-corrosion heat preservation pipe 4, the front end of the anti-corrosion heat preservation pipe 4 is sealed and connected with the top of the exhaust port of the chimney 1 through the flange 2, and the anti-corrosion heat preservation pipe 4 is provided with an exhaust valve A3, the waste gas purification device is made up of absorption chamber 8 and decomposition chamber 10, holds reaction liquid 16 in the absorption chamber 8, and reaction liquid 16 is mainly the alkali solution of sodium, potassium or the carbonate solution of sodium, potassium or this alkali solution and The mixed solution of carbonate solution reacts with carbon dioxide to generate sodium or potassium bicarbonate solution. In the decomposition chamber 10, it is the corresponding bicarbonate solution after the reaction in the absorption chamber 8. After the reaction in the absorption chamber 8, the gas pressure Press down into the decomposition chamber 10, and the solution in the decomposition chamber 10 enters the absorption chamber 8 under the action of its own weight after being pyrolyzed. In the device setting, ensure that the height of the bottom of the decomposition chamber 10 is higher than the upper liquid level in the absorption chamber 8 .
吸收室8底部与废气热分离装置5通过防腐导气管6连接,防腐导气管6的一端与废气热分离装置5相连接,防腐导气管6的另一端伸入到吸收室8内底部,吸收室8的底部与分解室10的底部通过冷凝管19连通,冷凝管19上装有冷凝器18,吸收室8和冷凝器18之间的冷凝管上设有控制阀B17,分解室10置于加热箱9中,废气热分离装置5与加热箱9通过防腐导热管7连接,防腐导热管7一端与废气热分离装置5连接,防腐导热管7的另一端伸入到加热箱9中,尾气收集处理装置15与吸收室8顶端通过防腐导气管14连接,防腐导气管14上设有控制阀A13,分解室10内设有温度传感器40,吸收室8顶端上设有降压排气管11,降压排气管11上设有排气阀B12,所述搅拌装置包括桩机架29、搅拌轴32、多个搅拌叶片33、固化剂储藏容器31和固化剂输送管30,搅拌轴32竖直附着在桩机架29上,搅拌轴32与固化剂储藏容器31通过固化剂输送管30连接,所述多个搅拌叶片33固定在搅拌轴32上,所述气体泵入装置包括减压阀20、冷却抽气泵21、气体流量计22、导气管23、控制阀C24、高压气瓶25、压力泵26、高压管36和压力控制阀37,分解室10顶端与高压气瓶25顶端通过导气管23密封连接,从分解室10到高压气瓶25的方向上,导气管23上依次设有减压阀20、冷却抽气泵21、气体流量计22和控制阀C24,其中减压阀20置于分解室10顶端和冷却抽气泵21之间,与分解室10顶端和冷却抽气泵21相邻,冷却抽气泵21置于减压阀20和气体流量计22之间,与减压阀20和气体流量计22相邻,控制阀C24置于气体流量计22和高压气瓶25顶端之间,与气体流量计22和高压气瓶25顶端相邻,压力泵26置于高压气瓶25顶端,多个导入管27插入地基土28中,所述多个导入管27分别与支管38连接,高压管36的一端与高压气瓶25的内顶端连通,另一端通过压力控制阀37与支管38连接。The bottom of the absorption chamber 8 is connected to the waste gas heat separation device 5 through the anti-corrosion air guide pipe 6, one end of the anti-corrosion air guide pipe 6 is connected to the waste gas heat separation device 5, and the other end of the anti-corrosion air guide pipe 6 extends into the bottom of the absorption chamber 8, and the absorption chamber The bottom of 8 communicates with the bottom of decomposition chamber 10 through condensation pipe 19. Condenser 18 is installed on condensation pipe 19. Control valve B17 is provided on the condensation pipe between absorption chamber 8 and condenser 18. Decomposition chamber 10 is placed in heating box. 9, the waste gas thermal separation device 5 is connected to the heating box 9 through the anti-corrosion heat-conducting tube 7, one end of the anti-corrosion heat-conducting tube 7 is connected to the exhaust gas thermal separation device 5, and the other end of the anti-corrosion heat-conducting tube 7 extends into the heating box 9, and the tail gas is collected and processed The device 15 is connected to the top of the absorption chamber 8 through an anti-corrosion air guide pipe 14, the anti-corrosion air guide pipe 14 is provided with a control valve A13, the decomposition chamber 10 is provided with a temperature sensor 40, and the top of the absorption chamber 8 is provided with a pressure-reducing exhaust pipe 11 to reduce the pressure. Pressure exhaust pipe 11 is provided with exhaust valve B12, and described stirring device comprises pile frame 29, stirring shaft 32, a plurality of stirring blades 33, curing agent storage container 31 and curing agent delivery pipe 30, and stirring shaft 32 is vertical Attached to the pile frame 29, the stirring shaft 32 is connected with the curing agent storage container 31 through the curing agent delivery pipe 30, the plurality of stirring blades 33 are fixed on the stirring shaft 32, and the gas pumping device includes a pressure reducing valve 20 , cooling air pump 21, gas flow meter 22, air guide pipe 23, control valve C24, high-pressure gas cylinder 25, pressure pump 26, high-pressure pipe 36 and pressure control valve 37, decomposition chamber 10 top and high-pressure gas cylinder 25 top pass through air guide pipe 23 sealed connection, from the decomposition chamber 10 to the direction of the high-pressure gas cylinder 25, the air guide pipe 23 is provided with a pressure reducing valve 20, a cooling air pump 21, a gas flow meter 22 and a control valve C24 in sequence, wherein the pressure reducing valve 20 is placed Between the top of the decomposition chamber 10 and the cooling air pump 21, adjacent to the top of the decomposition chamber 10 and the cooling air pump 21, the cooling air pump 21 is placed between the decompression valve 20 and the gas flow meter 22, and is connected to the decompression valve 20 and the gas flow meter. The flowmeter 22 is adjacent, the control valve C24 is placed between the gas flowmeter 22 and the top of the high-pressure gas cylinder 25, adjacent to the top of the gas flowmeter 22 and the high-pressure gas cylinder 25, and the pressure pump 26 is placed at the top of the high-pressure gas cylinder 25, and more One introduction pipe 27 is inserted in the foundation soil 28, and described a plurality of introduction pipes 27 are respectively connected with branch pipe 38, and one end of high-pressure pipe 36 communicates with the inner top of high-pressure cylinder 25, and the other end is connected with branch pipe 38 through pressure control valve 37.
吸收室8、分解室10和加热箱9均为密封容器,吸收室8中盛放反应液16,分解室10底部高度不低于吸收室8中反应液16的上平面,吸收室8采用防腐材料制作,分解室10采用防腐且导热的材料制作。The absorption chamber 8, the decomposition chamber 10 and the heating box 9 are all sealed containers. The reaction solution 16 is contained in the absorption chamber 8. The height of the bottom of the decomposition chamber 10 is not lower than the upper plane of the reaction solution 16 in the absorption chamber 8. The absorption chamber 8 adopts anti-corrosion Made of materials, the decomposition chamber 10 is made of anti-corrosion and heat-conducting materials.
搅拌叶片33通过螺栓或焊接连接在搅拌轴32的低端,搅拌轴32为中空状的,所述多个搅拌叶片33为对称排布,可为2或3层,在搅拌轴低端的两层搅拌叶片33之间的搅拌轴32上设有固化剂喷口34。导入管27上设有双排通气孔39,导入管27与支管38相连,支管38上方的地基土28表面覆设有密封膜35。The stirring blades 33 are connected to the lower end of the stirring shaft 32 by bolts or welding, the stirring shaft 32 is hollow, and the plurality of stirring blades 33 are arranged symmetrically, which can be 2 or 3 layers. A curing agent spout 34 is provided on the stirring shaft 32 between the stirring blades 33 of the layers. The introduction pipe 27 is provided with double rows of ventilation holes 39 , the introduction pipe 27 is connected with the branch pipe 38 , and the surface of the foundation soil 28 above the branch pipe 38 is covered with a sealing film 35 .
利用工业废气热加固软土地基的具体实施方式:The specific implementation method of using industrial waste gas heat to strengthen the soft soil foundation:
虽然下述各个实施例中的采用的是碳酸氢钠溶液或碳酸氢钾溶液,但也可以使用其他碳酸氢盐溶液,该相应碳酸氢盐是碳酸反应液16反应以后得到的被压到分解室10中的溶液中的。温度传感器40在分解室10中,所以温度传感器40所显示温度即为分解室10中的环境温度,而碳酸氢盐在该温度下即可分解。Although what adopt in following each embodiment is sodium bicarbonate solution or potassium bicarbonate solution, also can use other bicarbonate solutions, this corresponding bicarbonate is that carbonic acid reaction solution 16 reacts and obtains after being pressed into decomposition chamber 10 in solution. The temperature sensor 40 is in the decomposition chamber 10, so the temperature displayed by the temperature sensor 40 is the ambient temperature in the decomposition chamber 10, and bicarbonate can be decomposed at this temperature.
实施例1Example 1
a.利用防腐保温管4将除尘后的工业废气热传入工业废气热分离装置5中,分离后的废气通过防腐导气管6通入吸收室8中,分离后的热量通过防腐导热管7导入加热箱9中,a. Use the anti-corrosion insulation pipe 4 to transfer the industrial waste gas heat after dust removal into the industrial waste gas thermal separation device 5, and the separated waste gas passes into the absorption chamber 8 through the anti-corrosion air guide pipe 6, and the separated heat is introduced through the anti-corrosion heat conduction pipe 7 heating box 9,
b.在吸收室8中加入的反应液16为氢氧化钠溶液,关闭排气阀B12,打开控制阀A13,过量二氧化碳气体与溶液充分反应生成饱和碳酸氢钠溶液后,关闭控制阀A13和减压阀20,打开控制阀B17和控制阀C24,废气将吸收室8的饱和碳酸氢钠溶液通过冷凝管19压入分解室10中,溶液完全进入分解室10后,关闭控制阀B17,打开控制阀A13,b. the reaction solution 16 added in the absorption chamber 8 is sodium hydroxide solution, close the exhaust valve B12, open the control valve A13, after excessive carbon dioxide gas and solution fully react to generate saturated sodium bicarbonate solution, close the control valve A13 and reduce Pressure valve 20, open control valve B17 and control valve C24, the exhaust gas will press the saturated sodium bicarbonate solution in the absorption chamber 8 into the decomposition chamber 10 through the condensation pipe 19, after the solution completely enters the decomposition chamber 10, close the control valve B17, open the control valve valve A13,
c.分解室10中的饱和碳酸氢钠溶液在热的作用下分解出二氧化碳气体,其中分解室10中的温度不低于相应碳酸氢钠溶液分解的最低温度,然后关闭压力控制阀37,冷却抽气泵21将二氧化碳气体通过导气管23通入高压气瓶25中,其中相应碳酸氢钠溶液是反应液16反应以后得到的,并被废气压到分解室10中的。温度传感器40在分解室10中,所以温度传感器40所显示温度即为分解室10中的环境温度,而碳酸氢钠在该温度下即可分解,C. the saturated sodium bicarbonate solution in the decomposition chamber 10 decomposes carbon dioxide gas under the effect of heat, wherein the temperature in the decomposition chamber 10 is not lower than the minimum temperature of the corresponding sodium bicarbonate solution decomposition, then close the pressure control valve 37, cooling Aspirator 21 passes carbon dioxide gas in the high-pressure gas cylinder 25 through the air guide tube 23, wherein the corresponding sodium bicarbonate solution is obtained after the reaction of the reaction solution 16, and is compressed into the decomposition chamber 10 by the waste gas. Temperature sensor 40 is in the decomposition chamber 10, so the displayed temperature of temperature sensor 40 is the ambient temperature in the decomposition chamber 10, and sodium bicarbonate can be decomposed at this temperature,
d.气体流量计22低于正常流量的10%时,关闭控制阀C24,打开控制阀B17和控制阀A13和减压阀20,分解室10中的溶液在重力作用下经冷凝管19和冷凝器18流入吸收室8中,然后关闭控制阀B17,d. When the gas flow meter 22 is lower than 10% of the normal flow rate, close the control valve C24, open the control valve B17, the control valve A13 and the pressure reducing valve 20, and the solution in the decomposition chamber 10 passes through the condensation pipe 19 and condenses under the action of gravity. The device 18 flows into the absorption chamber 8, and then closes the control valve B17,
e.重复实施步骤a-d,不断产生二氧化碳气体。e. Repeat steps a-d to continuously generate carbon dioxide gas.
f.根据搅拌叶片33的半径和搅拌轴32的提升速度,设置活性氧化镁粉末输送率,通过地基土搅拌装置中的固化剂输送管30、中空状搅拌轴32和固化剂喷口34将活性氧化镁粉末从固化剂储藏容器31分布在地基土28,并通过搅拌叶片33将活性氧化镁粉末和地基土28均匀搅拌,f. According to the radius of the stirring blade 33 and the lifting speed of the stirring shaft 32, the active magnesium oxide powder delivery rate is set, and the active oxidation is activated by the curing agent delivery pipe 30, the hollow stirring shaft 32 and the curing agent spout 34 in the foundation soil stirring device. The magnesium powder is distributed on the foundation soil 28 from the curing agent storage container 31, and the active magnesium oxide powder and the foundation soil 28 are evenly stirred by the stirring blade 33,
g.将导入管27垂直插入地基土28中,并连接到支管38上,打开压力控制阀37和压力泵26,将高压气瓶25中的二氧化碳通过高压管36、支管38、导入管27和通气孔39导入到地基土28中,地基土28的碳化反应需在密封膜35下进行生成碳酸镁。g. the introduction pipe 27 is vertically inserted into the foundation soil 28, and connected to the branch pipe 38, the pressure control valve 37 and the pressure pump 26 are opened, and the carbon dioxide in the high-pressure cylinder 25 is passed through the high-pressure pipe 36, the branch pipe 38, the introduction pipe 27 and the The ventilation hole 39 is introduced into the foundation soil 28, and the carbonization reaction of the foundation soil 28 needs to be carried out under the sealing film 35 to generate magnesium carbonate.
实施例2Example 2
a.利用防腐保温管4将除尘后的工业废气热传入工业废气热分离装置5中,分离后的废气通过防腐导气管6通入吸收室8中,分离后的热量通过防腐导热管7导入加热箱9中,a. Use the anti-corrosion insulation pipe 4 to transfer the industrial waste gas heat after dust removal into the industrial waste gas thermal separation device 5, and the separated waste gas passes into the absorption chamber 8 through the anti-corrosion air guide pipe 6, and the separated heat is introduced through the anti-corrosion heat conduction pipe 7 heating box 9,
b.在吸收室8中加入的反应液16为碳酸钠溶液,关闭排气阀B12,打开控制阀A13,过量二氧化碳气体与溶液充分反应生成饱和碳酸氢钠溶液后,关闭控制阀A13和减压阀20,打开控制阀B17和控制阀C24,废气将吸收室8的饱和碳酸氢钠溶液通过冷凝管19压入分解室10中,溶液完全进入分解室10后,关闭控制阀B17,打开控制阀A13,b. the reaction solution 16 added in the absorption chamber 8 is a sodium carbonate solution, close the exhaust valve B12, open the control valve A13, after the excess carbon dioxide gas and the solution fully react to generate saturated sodium bicarbonate solution, close the control valve A13 and reduce pressure Valve 20, open the control valve B17 and control valve C24, the exhaust gas will press the saturated sodium bicarbonate solution in the absorption chamber 8 into the decomposition chamber 10 through the condensation pipe 19, after the solution completely enters the decomposition chamber 10, close the control valve B17, open the control valve A13,
c.分解室10中的饱和碳酸氢钠溶液在热的作用下分解出二氧化碳气体,其中分解室10中的温度不低于相应碳酸氢钠溶液分解的最低温度,然后关闭压力控制阀37,冷却抽气泵21将二氧化碳气体通过导气管23通入高压气瓶25中,其中相应碳酸氢钠溶液是反应液16反应以后得到的,并被废气压到分解室10中的。温度传感器40在分解室10中,所以温度传感器40所显示温度即为分解室10中的环境温度,而碳酸氢钠溶液在该温度下即可分解,C. the saturated sodium bicarbonate solution in the decomposition chamber 10 decomposes carbon dioxide gas under the effect of heat, wherein the temperature in the decomposition chamber 10 is not lower than the minimum temperature of the corresponding sodium bicarbonate solution decomposition, then close the pressure control valve 37, cooling Aspirator 21 passes carbon dioxide gas in the high-pressure gas cylinder 25 through the air guide tube 23, wherein the corresponding sodium bicarbonate solution is obtained after the reaction of the reaction solution 16, and is compressed into the decomposition chamber 10 by the waste gas. The temperature sensor 40 is in the decomposition chamber 10, so the displayed temperature of the temperature sensor 40 is the ambient temperature in the decomposition chamber 10, and the sodium bicarbonate solution can be decomposed at this temperature,
d.气体流量计22低于正常流量的10%时,关闭控制阀C24,打开控制阀B17和控制阀A13和减压阀20,分解室10中的溶液在重力作用下经冷凝管19和冷凝器18流入吸收室8中,然后关闭控制阀B17,d. When the gas flow meter 22 is lower than 10% of the normal flow rate, close the control valve C24, open the control valve B17, the control valve A13 and the pressure reducing valve 20, and the solution in the decomposition chamber 10 passes through the condensation pipe 19 and condenses under the action of gravity. The device 18 flows into the absorption chamber 8, and then closes the control valve B17,
e.重复实施步骤a-d,不断产生二氧化碳气体。e. Repeat steps a-d to continuously generate carbon dioxide gas.
f.根据搅拌叶片33的半径和搅拌轴32的提升速度,设置活性氧化镁粉末输送率,通过地基土搅拌装置中的固化剂输送管30、中空状搅拌轴32和固化剂喷口34将活性氧化镁粉末从固化剂储藏容器31分布在地基土28,并通过搅拌叶片33将活性氧化镁粉末和地基土28均匀搅拌,f. According to the radius of the stirring blade 33 and the lifting speed of the stirring shaft 32, the active magnesium oxide powder delivery rate is set, and the active oxidation is activated by the curing agent delivery pipe 30, the hollow stirring shaft 32 and the curing agent spout 34 in the foundation soil stirring device. The magnesium powder is distributed on the foundation soil 28 from the curing agent storage container 31, and the active magnesium oxide powder and the foundation soil 28 are evenly stirred by the stirring blade 33,
g.将气体导入管27垂直插入地基土28中,并连接到支管38上,打开压力控制阀37和压力泵26,将高压气瓶25中的二氧化碳通过高压管36、支管38、导入管27和通气孔39导入到地基土28中,地基土28的碳化反应需在密封膜35下进行生成碳酸镁。g. Insert the gas introduction pipe 27 vertically into the foundation soil 28, and connect it to the branch pipe 38, open the pressure control valve 37 and the pressure pump 26, and pass the carbon dioxide in the high-pressure gas cylinder 25 through the high-pressure pipe 36, the branch pipe 38, and the introduction pipe 27 And air hole 39 is imported in foundation soil 28, and the carbonization reaction of foundation soil 28 needs to carry out generation magnesium carbonate under sealing film 35.
实施例3Example 3
a.利用防腐保温管4将除尘后的工业废气热传入工业废气热分离装置5中,分离后的废气通过防腐导气管6通入吸收室8中,分离后的热量通过防腐导热管7导入加热箱9中,a. Use the anti-corrosion insulation pipe 4 to transfer the industrial waste gas heat after dust removal into the industrial waste gas thermal separation device 5, and the separated waste gas passes into the absorption chamber 8 through the anti-corrosion air guide pipe 6, and the separated heat is introduced through the anti-corrosion heat conduction pipe 7 heating box 9,
b.在吸收室8中加入的反应液16为氢氧化钾溶液,关闭排气阀B12,打开控制阀A13,过量二氧化碳气体与溶液充分反应生成饱和碳酸氢钾溶液后,关闭控制阀A13和减压阀20,打开控制阀B17和控制阀C24,废气将吸收室8的饱和碳酸氢钾溶液通过冷凝管19压入分解室10中,溶液完全进入分解室10后,关闭控制阀B17,打开控制阀A13,b. the reaction solution 16 added in the absorption chamber 8 is potassium hydroxide solution, close the exhaust valve B12, open the control valve A13, after the excess carbon dioxide gas and the solution fully react to generate saturated potassium bicarbonate solution, close the control valve A13 and reduce Pressure valve 20, open control valve B17 and control valve C24, the exhaust gas will press the saturated potassium bicarbonate solution in the absorption chamber 8 into the decomposition chamber 10 through the condensation pipe 19, after the solution completely enters the decomposition chamber 10, close the control valve B17, open the control valve valve A13,
c.分解室10中的饱和碳酸氢钾溶液在热的作用下分解出二氧化碳气体,其中分解室10中的温度不低于相应碳酸氢钾溶液分解的最低温度,然后关闭压力控制阀37,冷却抽气泵21将二氧化碳气体通过导气管23通入高压气瓶25中,其中相应碳酸氢钾溶液是反应液16与废气反应以后得到的,并被废气压到分解室10中的。温度传感器40在分解室10中,所以温度传感器40所显示温度即为分解室10中的环境温度,而碳酸氢钾溶液在该温度下即可分解,C. the saturated potassium bicarbonate solution in the decomposition chamber 10 decomposes carbon dioxide gas under the effect of heat, wherein the temperature in the decomposition chamber 10 is not lower than the minimum temperature of corresponding potassium bicarbonate solution decomposition, then closes the pressure control valve 37, cools Aspirator 21 passes carbon dioxide gas in the high-pressure gas bottle 25 through air guide tube 23, and wherein corresponding potassium bicarbonate solution is obtained after reaction liquid 16 and waste gas reaction, and is pushed in the decomposition chamber 10 by waste gas. The temperature sensor 40 is in the decomposition chamber 10, so the temperature displayed by the temperature sensor 40 is the ambient temperature in the decomposition chamber 10, and the potassium bicarbonate solution can be decomposed at this temperature,
d.气体流量计22低于正常流量的10%时,关闭控制阀C24,打开控制阀B17和控制阀A13和减压阀20,分解室10中的溶液在重力作用下经冷凝管19和冷凝器18流入吸收室8中,然后关闭控制阀B17,d. When the gas flow meter 22 is lower than 10% of the normal flow rate, close the control valve C24, open the control valve B17, the control valve A13 and the pressure reducing valve 20, and the solution in the decomposition chamber 10 passes through the condensation pipe 19 and condenses under the action of gravity. The device 18 flows into the absorption chamber 8, and then closes the control valve B17,
e.重复实施步骤a-d,不断产生二氧化碳气体。e. Repeat steps a-d to continuously generate carbon dioxide gas.
f.根据搅拌叶片33的半径和搅拌轴32的提升速度,设置生石灰输送率,通过地基土搅拌装置中的固化剂输送管30、中空状搅拌轴32和固化剂喷口34将生石灰从固化剂储藏容器31分布在地基土28,并通过搅拌叶片33将生石灰和地基土28均匀搅拌,f. according to the radius of the stirring blade 33 and the lifting speed of the stirring shaft 32, the quicklime delivery rate is set, and the quicklime is stored from the curing agent by the curing agent delivery pipe 30, the hollow stirring shaft 32 and the curing agent spout 34 in the foundation soil stirring device The container 31 is distributed on the foundation soil 28, and the quicklime and the foundation soil 28 are uniformly stirred by the stirring blade 33,
g.将气体导入管27垂直插入地基土28中,并连接到支管38上,打开压力控制阀37和压力泵26,将高压气瓶25中的二氧化碳通过高压管36、支管38、导入管27和通气孔39导入到地基土28中,地基土28的碳化反应需在密封膜35下进行生成硅酸钙和碳酸钙。g. Insert the gas introduction pipe 27 vertically into the foundation soil 28, and connect it to the branch pipe 38, open the pressure control valve 37 and the pressure pump 26, and pass the carbon dioxide in the high-pressure gas cylinder 25 through the high-pressure pipe 36, the branch pipe 38, and the introduction pipe 27 And air hole 39 is imported in foundation soil 28, and the carbonization reaction of foundation soil 28 needs to carry out generation calcium silicate and calcium carbonate under sealing film 35.
实施例4Example 4
a.利用防腐保温管4将除尘后的工业废气热传入工业废气热分离装置5中,分离后的废气通过防腐导气管6通入吸收室8中,分离后的热量通过防腐导热管7导入加热箱9中,a. Use the anti-corrosion insulation pipe 4 to transfer the industrial waste gas heat after dust removal into the industrial waste gas thermal separation device 5, and the separated waste gas passes into the absorption chamber 8 through the anti-corrosion air guide pipe 6, and the separated heat is introduced through the anti-corrosion heat conduction pipe 7 heating box 9,
b.在吸收室8中加入的反应液16为氢氧化钠溶液和碳酸钠溶液的等比例混合液,关闭排气阀B12,打开控制阀A13,过量二氧化碳气体与溶液充分反应生成饱和碳酸氢钠溶液后,关闭控制阀A13和减压阀20,打开控制阀17和控制阀C24,废气将吸收室8的饱和碳酸氢钠溶液通过冷凝管19压入分解室10中,溶液完全进入分解室10后,关闭控制阀B17,打开控制阀A13,b. The reaction solution 16 added in the absorption chamber 8 is an equal proportion mixed solution of sodium hydroxide solution and sodium carbonate solution, and the exhaust valve B12 is closed, and the control valve A13 is opened, so that excess carbon dioxide gas and the solution fully react to generate saturated sodium bicarbonate After solution, close control valve A13 and decompression valve 20, open control valve 17 and control valve C24, waste gas will press the saturated sodium bicarbonate solution of absorption chamber 8 in the decomposition chamber 10 through condensation pipe 19, and solution enters decomposition chamber 10 completely After that, close the control valve B17, open the control valve A13,
c.分解室10中的饱和碳酸氢钠溶液在热的作用下分解出二氧化碳气体,其中分解室10中的温度不低于相应碳酸氢钠溶液分解的最低温度,然后关闭压力控制阀37,冷却抽气泵21将二氧化碳气体通过导气管23通入高压气瓶25中,其中相应碳酸氢钠溶液是反应液16反应以后得到的,并被废气压到分解室10中的。温度传感器40在分解室10中,所以温度传感器40所显示温度即为分解室10中的环境温度,而碳酸氢钠溶液在该温度下即可分解,C. the saturated sodium bicarbonate solution in the decomposition chamber 10 decomposes carbon dioxide gas under the effect of heat, wherein the temperature in the decomposition chamber 10 is not lower than the minimum temperature of the corresponding sodium bicarbonate solution decomposition, then close the pressure control valve 37, cooling Aspirator 21 passes carbon dioxide gas in the high-pressure gas cylinder 25 through the air guide tube 23, wherein the corresponding sodium bicarbonate solution is obtained after the reaction of the reaction solution 16, and is compressed into the decomposition chamber 10 by the waste gas. The temperature sensor 40 is in the decomposition chamber 10, so the displayed temperature of the temperature sensor 40 is the ambient temperature in the decomposition chamber 10, and the sodium bicarbonate solution can be decomposed at this temperature,
d.气体流量计22低于正常流量的10%时,关闭控制阀C24,打开控制阀B17和控制阀A13和减压阀20,分解室10中的溶液在重力作用下经冷凝管19和冷凝器18流入吸收室8中,然后关闭控制阀B17,d. When the gas flow meter 22 is lower than 10% of the normal flow rate, close the control valve C24, open the control valve B17, the control valve A13 and the pressure reducing valve 20, and the solution in the decomposition chamber 10 passes through the condensation pipe 19 and condenses under the action of gravity. The device 18 flows into the absorption chamber 8, and then closes the control valve B17,
e.重复实施步骤a-d,不断产生二氧化碳气体。e. Repeat steps a-d to continuously generate carbon dioxide gas.
f.根据搅拌叶片33的半径和搅拌轴32的提升速度,设置活性氧化镁粉末和生石灰等比例混合物输送率,通过地基土搅拌装置中的固化剂输送管30、中空状搅拌轴32和固化剂喷口34将活性氧化镁粉末和生石灰等比例混合物从固化剂储藏容器31分布在地基土28,并通过搅拌叶片33将活性氧化镁粉末和生石灰等比例的混合物和地基土28均匀搅拌,f. According to the radius of the stirring blade 33 and the lifting speed of the stirring shaft 32, the delivery rate of the mixture of active magnesium oxide powder and unslaked lime is set, through the solidifying agent delivery pipe 30, the hollow stirring shaft 32 and the solidifying agent in the foundation soil stirring device The spout 34 distributes the equal proportion mixture of active magnesium oxide powder and quicklime from the curing agent storage container 31 to the foundation soil 28, and the mixture of active magnesium oxide powder and quicklime equal proportion and the foundation soil 28 are evenly stirred by the stirring blade 33,
g.将气体导入管27垂直插入地基土28中,并连接到支管38上,打开压力控制阀37和压力泵26,将高压气瓶25中的二氧化碳通过高压管36、支管38、导入管27和通气孔39导入到地基土28中,地基土28的碳化反应需在密封膜35下进行生成硅酸钙、碳酸钙和碳酸镁。g. Insert the gas introduction pipe 27 vertically into the foundation soil 28, and connect it to the branch pipe 38, open the pressure control valve 37 and the pressure pump 26, and pass the carbon dioxide in the high-pressure gas cylinder 25 through the high-pressure pipe 36, the branch pipe 38, and the introduction pipe 27 And air hole 39 is imported in foundation soil 28, and the carbonization reaction of foundation soil 28 needs to carry out generation calcium silicate, calcium carbonate and magnesium carbonate under sealing film 35.
实施例5Example 5
a.利用防腐保温管4将除尘后的工业废气热传入工业废气热分离装置5中,分离后的废气通过防腐导气管6通入吸收室8中,分离后的热量通过防腐导热管7导入加热箱9中,a. Use the anti-corrosion insulation pipe 4 to transfer the industrial waste gas heat after dust removal into the industrial waste gas thermal separation device 5, and the separated waste gas passes into the absorption chamber 8 through the anti-corrosion air guide pipe 6, and the separated heat is introduced through the anti-corrosion heat conduction pipe 7 heating box 9,
b.在吸收室8中加入的反应液16为氢氧化钠溶液和碳酸钠溶液的1:3混合液,关闭排气阀B12,打开控制阀A13,过量二氧化碳气体与溶液充分反应生成饱和碳酸氢钠溶液后,关闭控制阀A13和减压阀20,打开控制阀B17和控制阀C24,废气将吸收室8的饱和碳酸氢钠溶液通过冷凝管19压入分解室10中,溶液完全进入分解室10后,关闭控制阀B17,打开控制阀A13,b. The reaction solution 16 added in the absorption chamber 8 is a 1:3 mixed solution of sodium hydroxide solution and sodium carbonate solution, the exhaust valve B12 is closed, the control valve A13 is opened, and the excess carbon dioxide gas reacts fully with the solution to generate saturated bicarbonate After the sodium solution, close the control valve A13 and the pressure reducing valve 20, open the control valve B17 and the control valve C24, the exhaust gas will press the saturated sodium bicarbonate solution in the absorption chamber 8 into the decomposition chamber 10 through the condenser pipe 19, and the solution will completely enter the decomposition chamber After 10, close the control valve B17, open the control valve A13,
c.分解室10中的饱和碳酸氢钠溶液在热的作用下分解出二氧化碳气体,其中分解室10中的温度不低于相应碳酸氢钠溶液分解的最低温度,然后关闭压力控制阀37,冷却抽气泵21将二氧化碳气体通过导气管23通入高压气瓶25中,其中相应碳酸氢钠溶液是反应液16反应以后得到的,并被废气压到分解室10中的。温度传感器40在分解室10中,所以温度传感器40所显示温度即为分解室10中的环境温度,而碳酸氢钠溶液在该温度下即可分解,C. the saturated sodium bicarbonate solution in the decomposition chamber 10 decomposes carbon dioxide gas under the effect of heat, wherein the temperature in the decomposition chamber 10 is not lower than the minimum temperature of the corresponding sodium bicarbonate solution decomposition, then close the pressure control valve 37, cooling Aspirator 21 passes carbon dioxide gas in the high-pressure gas cylinder 25 through the air guide tube 23, wherein the corresponding sodium bicarbonate solution is obtained after the reaction of the reaction solution 16, and is compressed into the decomposition chamber 10 by the waste gas. The temperature sensor 40 is in the decomposition chamber 10, so the displayed temperature of the temperature sensor 40 is the ambient temperature in the decomposition chamber 10, and the sodium bicarbonate solution can be decomposed at this temperature,
d.气体流量计22低于正常流量的10%时,关闭控制阀C24,打开控制阀B17和控制阀A13和减压阀20,分解室10中的溶液在重力作用下经冷凝管19和冷凝器18流入吸收室8中,然后关闭控制阀B17,d. When the gas flow meter 22 is lower than 10% of the normal flow rate, close the control valve C24, open the control valve B17, the control valve A13 and the pressure reducing valve 20, and the solution in the decomposition chamber 10 passes through the condensation pipe 19 and condenses under the action of gravity. The device 18 flows into the absorption chamber 8, and then closes the control valve B17,
e.重复实施步骤a-d,不断产生二氧化碳气体。e. Repeat steps a-d to continuously generate carbon dioxide gas.
f.根据搅拌叶片33的半径和搅拌轴32的提升速度,设置活性氧化镁粉末输送率,通过地基土搅拌装置中的固化剂输送管30、中空状搅拌轴32和固化剂喷口34将活性氧化镁粉末从固化剂储藏容器31分布在地基土28,并通过搅拌叶片33将活性氧化镁粉末和地基土28均匀搅拌,f. According to the radius of the stirring blade 33 and the lifting speed of the stirring shaft 32, the active magnesium oxide powder delivery rate is set, and the active oxidation is activated by the curing agent delivery pipe 30, the hollow stirring shaft 32 and the curing agent spout 34 in the foundation soil stirring device. The magnesium powder is distributed on the foundation soil 28 from the curing agent storage container 31, and the active magnesium oxide powder and the foundation soil 28 are evenly stirred by the stirring blade 33,
g.将气体导入管27垂直插入地基土28中,并连接到支管38上,打开压力控制阀37和压力泵26,将高压气瓶25中的二氧化碳通过高压管36、支管38、导入管27和通气孔39导入到地基土28中,地基土28的碳化反应需在密封膜35下进行生成碳酸镁。g. Insert the gas introduction pipe 27 vertically into the foundation soil 28, and connect it to the branch pipe 38, open the pressure control valve 37 and the pressure pump 26, and pass the carbon dioxide in the high-pressure gas cylinder 25 through the high-pressure pipe 36, the branch pipe 38, and the introduction pipe 27 And air hole 39 is imported in foundation soil 28, and the carbonization reaction of foundation soil 28 needs to carry out generation magnesium carbonate under sealing film 35.
Claims (9)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201310122135.0A CN103147434B (en) | 2013-04-10 | 2013-04-10 | Treatment system and method for consolidating soft soil foundation by utilizing industrial waste gas heat |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201310122135.0A CN103147434B (en) | 2013-04-10 | 2013-04-10 | Treatment system and method for consolidating soft soil foundation by utilizing industrial waste gas heat |
Publications (2)
Publication Number | Publication Date |
---|---|
CN103147434A CN103147434A (en) | 2013-06-12 |
CN103147434B true CN103147434B (en) | 2014-10-15 |
Family
ID=48545727
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201310122135.0A Active CN103147434B (en) | 2013-04-10 | 2013-04-10 | Treatment system and method for consolidating soft soil foundation by utilizing industrial waste gas heat |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN103147434B (en) |
Families Citing this family (10)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN103981854B (en) * | 2014-05-15 | 2015-10-28 | 东南大学 | A kind for the treatment of system for ground stabilization and carbonization piling method |
CN104018485B (en) * | 2014-06-18 | 2016-03-02 | 东南大学 | Bed course carbonization reinforcement means is filled out in changing of a kind of soft foundation |
CN108086297B (en) * | 2017-11-24 | 2018-10-02 | 东南大学 | A kind of ectopic activities magnesia carbonization curing sludge indigenous method |
CN108128991B (en) * | 2017-11-24 | 2018-11-09 | 东南大学 | A kind of ectopic activities magnesia carbonization curing sludge soil processing system |
WO2019100512A1 (en) | 2017-11-24 | 2019-05-31 | 东南大学 | Treatment system for ex-situ carbonization and solidification of silt soil using active magnesium oxide and method thereof |
CN109749745A (en) * | 2018-12-21 | 2019-05-14 | 西北农林科技大学 | A kind of method of using soil solidification solution to strengthen soil |
CN109797741B (en) * | 2019-03-28 | 2020-06-26 | 中通建工城建集团有限公司 | Carbonization stirring pile composite foundation and construction method thereof |
CN110512591B (en) * | 2019-09-02 | 2021-05-14 | 南京林业大学 | A kind of reinforcement method of vacuum preloaded pipe pile gas injection carbonization ultra-soft foundation |
CN110512589B (en) * | 2019-09-02 | 2021-06-29 | 南京林业大学 | A kind of super soft foundation solidification method of super soft foundation with vacuum dewatering and drainage combined with magnesium oxide carbonization |
CN117102222A (en) * | 2023-08-11 | 2023-11-24 | 江苏省环境科学研究院 | Portable contaminated soil in-situ quick emergency repair and reuse equipment |
Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN1053987A (en) * | 1990-02-15 | 1991-08-28 | 原满生 | Soil stabilizing apparatus |
CN101747902A (en) * | 2009-12-24 | 2010-06-23 | 福州大学 | Green and environment-friendly soil stabilizer taking industrial waste as raw material and application method thereof |
US8177909B2 (en) * | 2009-12-31 | 2012-05-15 | Calera Corporation | Methods and compositions using calcium carbonate |
CN102650126A (en) * | 2010-12-24 | 2012-08-29 | 东南大学 | Carbonization and solidification method for soil |
CN202562333U (en) * | 2012-04-17 | 2012-11-28 | 湖南广源麻业有限公司 | Industrial waste gas heat energy recycling device |
-
2013
- 2013-04-10 CN CN201310122135.0A patent/CN103147434B/en active Active
Patent Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN1053987A (en) * | 1990-02-15 | 1991-08-28 | 原满生 | Soil stabilizing apparatus |
CN101747902A (en) * | 2009-12-24 | 2010-06-23 | 福州大学 | Green and environment-friendly soil stabilizer taking industrial waste as raw material and application method thereof |
US8177909B2 (en) * | 2009-12-31 | 2012-05-15 | Calera Corporation | Methods and compositions using calcium carbonate |
CN102650126A (en) * | 2010-12-24 | 2012-08-29 | 东南大学 | Carbonization and solidification method for soil |
CN202562333U (en) * | 2012-04-17 | 2012-11-28 | 湖南广源麻业有限公司 | Industrial waste gas heat energy recycling device |
Also Published As
Publication number | Publication date |
---|---|
CN103147434A (en) | 2013-06-12 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN103147434B (en) | Treatment system and method for consolidating soft soil foundation by utilizing industrial waste gas heat | |
CN103203174B (en) | SO in a kind of trapping coal-fired plant flue gas 2and CO 2and the method for production chemical product | |
CN102773006A (en) | Device and process for cyclic capture of carbon dioxide by taking CaO as carrier | |
CN102786236B (en) | Device and method for capturing carbon dioxide in lime production process | |
CN102527225A (en) | Method for trapping carbon dioxide from smoke by renewable carbide slag | |
CN103145148A (en) | Method for mineralization-immobilization of carbon dioxide (CO2) through strengthening calcium-based solid wastes by using ammonia medium system | |
CN114570204B (en) | Method for dealkalizing and soil formation of organic amine-mediated red mud | |
CN106904647A (en) | A kind of CO2Method of the mineralising with seawater resources using coupling | |
CN112125550A (en) | Method for reinforcing recycled aggregate of waste concrete through open carbonization | |
CN104556155A (en) | Method for producing sodium carbonate by utilizing chlor-alkali ammonia-alkali tailings | |
KR20200034144A (en) | Method for Capturing, Storaging and Using Carbon Dioxide in Waste Gas of Cement Produciton Comprising the Using of Waste Heat of Cement Calcination Process | |
CN104740995A (en) | Fly-ash-based carbon dioxide curing agent and preparation method thereof | |
CN113617201A (en) | Method for trapping flue gas carbon dioxide by using nanofiltration seawater | |
CN202803106U (en) | Device for circularly catching carbon dioxide by taking CaO as carrier | |
TW201900263A (en) | Device And Treatment Method For Carbon Dioxide Capture and Utilization | |
CN102807392A (en) | Supercritical carbonization recycling equipment for reforming cement-based building materials | |
TW201836702A (en) | A method of capturing carbon dioxide in flue gas via high gravity carbonation equipment | |
CN114749008B (en) | A method of using MgCl2 to strengthen red mud dealkalization to absorb SO2 and utilize the slurry | |
CN117563392A (en) | A direct air carbon capture system and method | |
CN115417409B (en) | Method for reinforcing red mud carbon fixation through cooperation of solid wastes in multi-production industry | |
CN108261890B (en) | Integrated CO capture in flue gas2And N2Collecting device | |
CN101642667B (en) | Method for using cooling-tower circulating water as water used by flue gas desulfurization system | |
CN105523571A (en) | Method for processing mineralized organic amine and resource utilization used after carbon dioxide capture | |
CN102188893A (en) | Method for absorbing carbon dioxide in combustion product gases by using magnesium oxide | |
US8916118B2 (en) | CO2 and SO2 capture method |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
C06 | Publication | ||
PB01 | Publication | ||
C10 | Entry into substantive examination | ||
SE01 | Entry into force of request for substantive examination | ||
C14 | Grant of patent or utility model | ||
GR01 | Patent grant |