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双语推荐:气化

对两种气化工艺( Lurgi和 GSP)从气化方法、煤种、进料要求、气化炉构造及国产化、生产能力、气化炉开车、废水处理方面进行了比较。通过比较, GSP气化比Lurgi气化具有气化煤种更广泛、煤种适应性更强、气化炉构造简单、维修量小、生产能力大、开车快、废水量少且处理系统简单的优点, Lurgi气化比GSP气化具有简单的进料要求、高的设备国产化率、低的氧气消耗、运行业绩较多的优点。为选择气化方式时提供参考。
Two gasification process ( Lurgi and GSP ) were Compared through gasification methods, coal, feed requirements, gasifier structure and localization, production capacity, start-up and effluent treatment. There were some advantages in GSP gasification technology better than in Lurgi gasification, such as coal universality, more stronger adaptability, simple structure of gasifier, small amount of maintenance, large production capacity, driving fast, a small amount of waste water and easy processing, etc. . However, in terms of simple feed requirements, high equipment localization rate, low oxygen consumption and operational performance, there were more advantages in Lurgi gasification. A reference for choosing way of gasification was provided.

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梯度链条式生物质气化炉按照气化规律从空间上将生物质气化过程分为4个阶段,可实现对各气化阶段气化条件进行控制。为此,对梯度链条式生物质气化炉进行数值模拟,通过改变ER,计算出不同ER下床层顶部各组分的温度和浓度分布及炉膛气相的气化特性。模拟结果显示:气化合成气出口温度622.24℃;气化合成气中CO为13.81%、CH4为3.26%、C2H4为0.601%、C2H6为0.002%、CnHm为10.936%、H2为3.82%;碳转化效率为75.1%,低位热值为5 501k J/Nm3,气化效率为57.56%。该气化效果比下吸式固定床气化炉、固定床气化炉及鼓泡床气化炉空气气化效果好。
According to the biomass gasification discipline, biomass gasification process is divided into four stages in gra-dient chain biomass gasifier.Thus can control gasification conditions in different gasification stage.Mathematical modeling methods have been employed to simulate a gradient chain biomass gasifier, not only the temperature, concentra-tion distributing of the top of bed in different conditions, but also gasification character of gasifier chamber were calcula ted, by varying the ratio of actual air fuel ratio and stoichiometric air fuel ratio( ER) .The results showed that the tem-perature, concentration distributing( CO, CH4 , C2 H4 , Cn Hm , H2 ) , carbon conversion efficiency, HLV of the gas fuel, gasification efficiency vary in the range of 622.24℃,CO 13.81%,CH4 3.26%,C2 H4 0.601%,C2 H6 0.002%,Cn Hm 10.936%, H2 3.82%, 75.1%, 5501 kJ/Nm3 , 57.56%, and this effect of gasification better than downdraft fixed bed gasifier, a fixed-bed gasifier and bubbling bed gasif

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[目的]对中医气化模型的理论基础和临床应用进行探讨。[方法]从气化概念的内涵与外延、气化理论的原理、气化模型与人体生命的关系及临床应用等方面对中医气化模型的理论基础和临床应用分别进行论析。[结果]中医人体气化模型包涵了气、血、津、精等客观因素和神、魂、魄等主观因素,遵循气化之道,以五脏特异气化模型为中心来构建与运行,气化失常则导致诸项因素的改变,从而变生百病。故气化失常为诸病之根本,调畅气机,推动气化是治疗的关键。[结论]"气病为百病之先,诸病之变"、"调理气机、推动气化为百病之要",气化之道是中医学认知生命的原创思维,是中医理论的根和魂。
[Objective] Make theoretical discussion on the basis of Qi-transformation model and its clinical application.[Methods]We analyse the theoretical basis theory of Qi-transformation model and its clinical application from the concept extension, principle, relationship between the model and human life. [Results]Human life holographic transportation and transformation model encompasses objective factors as qi, blood, saliva, essence and other subjective factors such as spirit, soul. The model fol ows the theory of qi transformation and centers about the five internal organs-specific pneumatolysis model to construct and operate .If qi-transformation disorders, it wil result in the change of the factors and give rise to diseases. Thus qi-transformation disorder as the root of various diseases is the key to adjust and promote pneumatolysis. [Conclusion]The qi-disease is the first of entire diseases and the changes of entire diseases. Recuperating qi-activity and promoting pneumatolysis is the

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以新疆伊犁新天煤化工有限责任公司20亿m^3/a煤制天然气项目气化工艺方案的选择为例,介绍了流化床气化工艺、气化床(喷流床)气化工艺和移动床(固定床)气化工艺的技术特点;对比分析了Lurgi碎煤加压气化工艺、GSP气化工艺和Shell粉煤气化工艺的消耗指标。结果表明:①由于当地煤种成浆性较差,不宜采用Texaco水煤浆气化工艺;②从投资、运行、管理等方面综合考虑,在Lurgi,GSP,Shell3种工艺方案中,Lurgi碎煤加压气化工艺具有一定的优势。
Taking the purification process scheme of coal-made natural gas project with a capacity of 2 ×109 m3 /a in the Xintian Coal-Chemical Engi-neering Company Ltd.as an example, author has introduced the technical features of NHD process and low temperature methanol wash process ; has com-pared the Lurge process and Linde process with the Dalian Technology and Engineering University ’s process.Result indicates that:(1)The low tempera-ture methanol wash process is preferable for the purification process of large-sized coal-chemical engineering project;(2)Considering from aspects of in-vestment, energy consume, environment etc., the Linde process has a definite superiority among low temperature methanol wash processes.
生物质气化再燃是生物质能利用的较好方式之一.生物质气化再燃技术中,气化气及焦油的不同组成对再燃效果有所影响.自行设计搭建热功率为10 kW的上吸式生物质气化炉,进行典型生物质燃料木屑的气化实验,通过改变气化剂空气的量,研究氧气对生物质气化气及焦油成分的影响.实验结果表明,氧气量增加,气化气中主要组分的体积含量均有所增加,而焦油中占据主要比重的酚类物质相对含量减少.此研究为生物质气化再燃技术的开发提供一定的理论指导.
Biomass gasification for reburning is one kind of the most promising ways of biomass utilization.Different composition of syngas and tar will influence the NO reduction effect in the process of biomass gasification for reburning.A 10 kW updraft biomass gasifier was designed and built,and experiments on wood gasification were carried out to study the effect of oxygen content on the composition of syngas and tar.The relative content of the main gas species in the syngas rises with the air flow rate increase,but the relative content of phenolic compounds,which share a large part in the tar,declines with the air flow rate increase according to the experimental results. The study provides a theoretical guidance for the development of technology of biomass gasification for reburning.

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在对煤气化飞灰的物理化学性质、微观形貌、气化反应活性和粘附特性归纳分析的基础上,讨论了气化飞灰的形成机理及其气化过程中的结渣倾向性,并对气化过程中避免飞灰在气化炉内的结渣和在合成气冷却器积灰结垢的措施进行了介绍。最后对气化飞灰的研究热点问题进行了展望。
Based on the analyses of the ehemieal and physieal properties,miero-strueture,gasifieation re-aetivity and its adhere eharaeteristies,the formation and slagging meehanism of fly ashes were diseussed. And the eontrol measurements of avoiding fly slagging during gasifieation and deposition on synthetie gas eooler were reviewed further. Finally the key researeh point of the fly ashes was also put forward.

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近年来,由于世界能源与环境危机,生物质能作为一种清洁的、可再生的能源越来越受到世界的关注,其中生物质气化是利用生物质能最重要的方式之一。本文介绍了生物质气化技术的原理,生物质气化工艺及气化设备,并对影响生物质气化装置的优化设计的各种因素进行了分析与讨论,提出了生物质气化工艺过程亟待解决的问题,为生物质气化的发展提供了一定的参考。
Currently , the depletion of world''s energy and environmental problem produced by combustion of fossil fuels led to the search for alternative fuels.Biomass gasification attracted high interest due to its high conversion efficiency and low pollution.The principle , process and equipment of biomass gasification technology were briefly introduced , and the influencing factors of biomass gasification process optimization design were analyzed , which can be a reference for the in industrial development for the biomass gasification.

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为提高低热稳定性低阶煤的碎煤加压气化效果,采用新疆、河南等地碎煤加压气化工艺,研究低阶煤热稳定性对碎煤加压气化效果的影响。结果表明:低热稳定性低阶煤的单台气化炉氧负荷仅达到设计的70%左右,比高热稳定性低阶煤低40%。煤的热稳定性越低,粗煤气中煤粉含量越高,影响煤气水分离、变换等后续工艺。最后提出可通过研究不同粒度煤的热稳定性、确定最小入炉煤粒度、测定碎煤加压气化煤粉的粒度、改进碎煤加压气化除尘系统、选择合理的气化压力、采用气化工艺组合等提高低热稳定性低阶煤碎煤加压气化效果。
In order to improve the effects of low thermal stability and low-rank coal in crushed coal pressurized gasification, adopt the crushed coal pressurized gasification processes in Henan and Xinjiang Province,investigate the influence of thermal stability of low-rank coal on crushed coal pressurized gasification. The results show that single gasifier oxygen load can only reach about 70% of design load when use low stability and low-rank coal,about 40% less than the high stability and low-rank coal.Thermal stability of coal is lower and the higher dust content in raw gas affects the gas-water separation,it also influents the transform and follow-up processes.The effects of low thermal stability and low-rank coal in crushed coal pressurized gasification can be improved through investigating the thermal stability of different particle size of coal,determining minimum grain size of pulverized coal into the gasifier and the particle size of pulverized coal in the crushed coal pressurized gasif

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为研究气化熔融技术对国内城市生活垃圾的适应性,以气化熔融试验台为原型,从热化学平衡角度建立了气化熔融工艺模拟模型.通过研究我国11种混合城市生活垃圾的气化熔融性质,得到了满足气化熔融温度要求的垃圾最大含水率和最佳过量空气系数,并分析了垃圾热值对最大含水率的作用规律以及过量空气系数、含水率和氧浓度对气化产物的影响.结果表明,过量空气系数在0.3~0.4之间时,气化产物热值最高.随着垃圾含水率的升高,冷气效升高,气化和熔融温度降低.
In order to search the adaptability of gasification and melting technology to municipal solid waste(MSW)in China,a thermochemical model was proposed as a prototype of the gasification and melting test-bed. Through the study on the gasification and melting characteristics of 11 different MSWs,the maximum moisture con-tent and excess air coefficient for waste changing with heat value were obtained under fixed boundary temperature. The effects of excess air coefficient(α),moisture content(RMC) and oxygen concentration on syngas composition were discussed. The results indicate that a maximum heat value of syngas can be obtained when α is between 0.3 and 0.4. As the moisture content increased,the cold gas efficiency(RCGE)increased while the operation temperature decreased at the same time.

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为合理利用煤炭资源,提高企业经济效益,寻找企业可持续发展之路,开展了煤炭地下气化试验。介绍了矿井煤层气化试验自动点火技术在重庆中梁山煤电气有限公司矿业分公司北矿煤层气化试验中的应用情况。分析了矿井煤层气化的特殊性和煤层点火的可靠性、安全性,讨论了煤炭地下气化工程的点火思路、供电方案,对自动点火装置进行了设计,并阐述了煤炭地下气化的过程测控,以及所产生的社会、经济和环境效益,为今后矿井进行煤层气化试验提供了宝贵经验。
Underground coal gasification test was carried out in order to rationally utilize coal resources,imProve the economic efficiency of the enterPrise and search a sustainable develoPment road for it. This PaPer described the aPPlication of the automatic ignition technology in coal-seam gasification test in the north mine of the Mining ComPany of Chongqing Zhongliangshan Coal, Electricity and Gas Co. ,Ltd. ,. It analyzed the Particularities of coal-seam gasification and the reliability and security of coal-seam ignition,discussed the ignition thinking and Power suPPly scheme of underground coal gasification and the design of the automatic ignition device,and exPounded the Process monitoring and control of underground coal gasification as well as its social,economic and environmental benefits,all of these Provided valuable exPerience for mine coal-seam gasification test in the future.

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