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英文原文及翻译

英文原文及翻译
英文原文及翻译

Characterization of bio-oil from induction-heating pyrolysis of food-processing sewage sludges using chromatographic analysis (可搜到原文)

利用色谱法分析感应加热热解食品加工污泥中生物油特征

Wen-Tien Tsai a,*, Mei-Kuei Lee b, Jeng-Hung Chang b, Ting-Yi Su b, Yuan-Ming Chang a

a Graduate Institute of Bioresources, National Pingtung University of Science and Technology, Pingtung 912, Taiwan

b Department of Environmental Engineering and Science, Chia Nan University of Pharmacy and Science, Tainan 717,

Taiwan

摘要:在这项研究中,利用气相色谱分析-质谱法(GC-MS)分析了热解生物油和来自感应加热技术热解工业污水污泥产生的气体的分数。使用从25到500℃加热速率为300℃/min,低温冷凝氮气中的挥发分得到了液体产品。分析结果表明:热解生物油是非常复杂的有机化合物的混合物和含有大量的氮氧化物/或含氧化合物,如脂肪烃类物质、酚类化合物、吡啶类、吡咯、胺类、酮类,等等。目前污水污泥中的微生物含有来自蛋白质和核酸纹理的有机碳氢化合物含有氮/或氧。不凝性挥发组分由氮氮氧化物和含氧的化合物组成,但所载小分数为酚类化合物、1H-吲哚和脂肪羧酸。另一方面,通过气相色谱法-热导检测器(GC-TCD)进行分析得出不凝气体产品中的成分主要是二氧化碳、一氧化碳和甲烷。

关键字:污水污泥;热解油;气相色谱-质谱法

介绍

为了应对全球气候变暖和化石燃料价格飙升,近年来生物质资源的能源利用已引起广泛关注,因为这种替代能源将难以放出有害空气污染物(如硫氧化物和有毒重金属)和不作为化石燃料相比增加净温室气体(即CO2)排放到大气中。这一发展的同时,产生的活性污泥对于城市污水污泥的处理和处置是严重问题及其对环境和人类健康的影响。生物废料传统上被植入土壤为农业应用(Fytili and Zabaniotou,2008).然而,由于市民洞察到有毒污染物和污水污泥中所载的病原体可能有不利影响,该方法引起了越来越多地市民的关注。由于不断增加的污泥管理成本,污水污泥最近已用作用于能量在所有产业生产的生物质资源(Rulkens,2008)。

在热化学技术中,热解已被广泛用于将生物质资源转化为可燃气体、生物油和焦炭。最近技术进一步证实了因为液体产品的产量增加了在(1)很高的加热速率及其加工条件(>100℃/min),(2)研磨得生物饲料(< 1mm),(3)严格控制温度(大约500℃)和(4)快速冷却的热解蒸气,得到生物原油产品(Bridgwater et al.,1999;Demirbas,2001;McKendry,2002;Gross et al.,2003)。热解产物从生物质资源的利用,这种气体可以视为气体燃料,而非水相生物油可用于作为液体燃料或原料化学品。在这方面,热解一直被视为一种可用的替代技术,污水污泥转化为生物燃料和有价值的化学品(Campbell and Bridle,1986; Werther and Ogada,1999)。污水污泥的热解机理是一个复杂的过程,因为同时众多的降解反应的发生可能与异类生物量(Cones et al.,1998)。其中包含可生物降解的有机物质,死掉的细菌和非生物降解分数。

为了更好地理解从污水污泥热解过程中产生的生物油产品制造的化学成分,在气相色谱-质谱(GC-MS)的基础上进行了几项研究。利用热重分析法-质谱联用仪(TGA-MS),Conesa et al. (1998)研

究了不同污水厂污泥从城市废水处理厂在升温速率20℃/min,产生大量的热降解C1-C4烃类,乙酸,等。Dominguez et al.(2003,2005,2006)调查产生的不同的城市生活污水的微波热解油馏分的表征污泥在高升温速率从167到300℃/min,识别不同种类的有机化合物:对于脂肪族、酸、酯、酰胺、腈、类固醇激素和多环芳烃(PAHs)。Fullana et al. (2003,2005)从社区废水处理厂取得污泥在卧式反应器炉中加热至850或700℃/min热解,展示有机化合物生物油中确定已被分为速度轻烃(如苯、甲苯)和半挥发性化合物(如苯甲腈、多环芳烃),大多属于氮氧化物化合物,如腈吡啶类、酰胺类、胺类和多环芳烃等化合物。Shen and Zhang (2003)也热解城市污水污泥在低温度(300-600℃)流化床上的7℃/min至500℃加热速度和进一步确定生物油成分的气相色谱-质谱法,表明热解油是复杂的混合物组成的沥青质、脂肪族、芳香烃和双星。Karayildirim et al.(2006年) 调查了在摇床上的7℃/min 至500℃,加热速度固定石油化工废水处理厂的污泥的热解和鉴定的生物油和分别使用TGA-MS和气相色谱法-热导检测器(GC-TCD),热解气体产品,指示热解油中含有大量的脂肪族化合物和气态产品主要是CO、CO2、氢和甲烷。Dominguez et al. (2007)也报道产生从电炉在升高的温度(即1000℃) 和高升温速率(约100℃/min) 在城市污水厂污泥的热解气体的特点。它被发现,气态的分数在热解过程中产生的氢含量高和湿生污泥气化明显高于干污泥的热解。Zhai等(2008)最近描述了从直径不同,城市污水厂污泥的热解产品的特点。他们主要确定化合物在生物油的组成包括芳香环分支链和长长的直的烃链联系在一起。

在以往的研究(Tsai et al.,2006,2007),式感应加热技术是适合于农业废弃物快速热解(即水稻稻壳、稻草,甘蔗蔗渣和椰子壳)。它被发现由此产生-生物油含有大量的水和较少的内容的羰基氧合脂肪烃合成。进一步,从食品加工工厂的三个污水污泥的热解研究了在感应加热炉,显示出变异生物油的产量和及其特点(即pH值、水分含量、元素分析、和低热值)不是那么重要的三个污水厂污泥的实验条件(Tsai et al.,2009)。这项工作的目的是来表征成分的挥发馏分,其中三个食品加工污水污泥处理中指定的感应加热热解条件下,用色谱方法生产(即气相色谱-质谱和气相色谱法-热导检测器)。因此,挥发组分样品包括的不凝性气体和可凝性生物油产品收集的低温系统(-10℃)在这项研究。

2.实验

2.1原料

实验运行的初始原料取自三个污水厂污泥分别是果糖制造、牛奶衍生物和啤酒酿造的工厂,被指定为标志污泥“X”、污泥“Y”和污泥“Z”。为了消除大部分的水分,将这些污泥在阳光下晒干,然后去除杂质(比如,碎石)。污水厂污泥在水平固定流化床反应器中,它由一种高频率发生器加热快速热解制备脱挥发分分数样品(即感应加热)如以前报告(Tsai et al.,2006,2007)。快速热解系统的实验条件如下:热解温度从室温到500℃、300℃/min,加热速率和氮气流量1000 cm3/min不等。由此产生的热解气体产品立即被冷却并冷凝通过操作低温循环浴在10℃与乙二醇/水的解决办法。由此产生的生物油然后被从耐热玻璃真空收集器,良好的绝缘情况,防止它蒸发。凝组分都含有大量的冷凝水。它们的C/H/N分别是5.4/4.9/1.7、6.4/2.8/2.3和5.3/0.7/1.3由重量(Tsai et al.,2009),分别得到的果糖制造污泥、牛奶制造污泥和啤酒酿造的污泥热解。这一结果与污水厂污泥的最终分析一致(Tsai et al.,2009)。

2.2热解实验

液化作为快速热解的污水污泥水平固定床反应堆的准备,由高频发生器加热(例如:感应热),此前报道(Tsai et al.,2006,2007)。快速热解系统的实验条件如下:热解温度范围从室温300℃~500℃ /min 升温速率,氮流量为1000cm3/min。由此产生的热解气体产品立即冷却和冷凝操作低温循环浴10℃与乙二醇/水的解决方案。用从派热克斯玻璃真空收集器收集生物油,它良好的绝缘防止它蒸发,可压缩的分数包含大量的凝聚水。他们的C/H/N质量比为5.4/4.9/1.7,2.8/2.3/6.4和5.3/0.7/1.3(Tsai et al.,2009).,热解分别获得果糖制造污泥、牛奶制造污泥和啤酒加工污泥。这个结果支持了污水污泥的最终分析((Tsai et al.,2009).。

2.3热解产品的特性

气相色谱/质谱(GC/MS)光谱分析对热解油进行了与惠普HP5890 系列二气相色谱仪配备-惠普HP-5972A质量选择检测器(MS)与离子源的电子碰撞在70eV,使用0.25mm内径0.25 lm薄膜厚度HP-1MS毛细管柱(固定相:100%制法)。温度程序进行如下:40℃(初始温度;保持5min)→(升温速率在5℃/min)→200℃(中间温度;保持5min)→(加热速度10℃ /min)→350℃ (最终温度;保持2min)。喷油器温度和检测器温度分别为250℃,280 ℃。石油样品(0.2ul)是一个汉密尔顿注射器注射。纯度为99.999%的氦用作载气以恒定流量的1mL/min。操作的在扫描模式和质量范围45-500a.m.u。化合物初步确定了通过比较他们的质谱和保留时间与搜索文件(HP MS ChemStation)。证明Dominguez et al .(2003、2005、2006),半定量的数据确定化合物可以进一步通过集成处理的总离子色谱图(TIC)和计算每个峰的面积百分比为目的的比较。

为了检查的不凝分数由此产生的气相焦油产品,气相色谱-质谱(如上所述)是用于分析热解气体收集10 l泰德拉袋。采用温度程序如下:初始的和最终的温度为35和200℃,分别初始和最终的是10min和5min,分别和加热率为10℃。喷油器温度150 ℃和气体样本的汉密尔顿注射器注射1mL。另一方面,定量成分的不凝气体收集在3l泰德拉袋使用安捷伦6820型气相色谱仪分析了GC系统热导检测器。不锈钢填充柱(4.5m,1/8,60/80-1000;USA Supelco Inc.),被用来量化(如永久气体:CO 和CO2)和光碳氢化合物(如:食品加工生物污泥CH4)热解。温度进行气相色谱-热导检测器如下:40℃(初始温度;保持5min)→(加热20℃/min)→160℃(最后温度;保持9min)。喷油器温度和检测器温度分别为250 ℃、280 ℃。气体样品是汉密尔顿不漏气的注射器注射。纯度为99.9999%的氦用作载气以恒定流量的30mL/min。校准气体混合物(包括H2、O2、CO、CO2和CH4、N2)从斯科特获得专业气体(48;Supelco Inc.)、USA)被用来确定CO的浓度、二氧化碳和甲烷中包含非冷凝气体从食品加工生物污泥热解产物。

3结果与讨论

3.1成分的热解生物油

正如前面研究(Tsai et al.,2009),从热解生物油污水污泥应该包含高氮的成分和含氧碳氢化合物的元素分析数据显示。这些有机成分可以或许污水污泥的来源,因为氮气和氧气的蛋白质氨基酸(和/或)可以发现出现在位于污泥(Gomez-Rico et al .,2005)。在这个工作,使用气相色谱/质谱法(气相色谱-质谱)分析热解生物油的特性可能是有益的,因为生物油的氮氧化物(NO x)来源而被利用作为一个潜在的生物燃料热。

表1列出了确定成分及其相对结果面积(%)。总化合物中确定这项工作达53.6%,占总数的38.2%和22.0%峰值分别是污泥热解的X,Y污泥和污泥Z。显然,这种未知热解油和复杂的有机化合物的混合物,探测器的设置,主要是由于缺乏一个合适的校准的标准混合物。证明Dominguez et al .(2003、2005、2006),构成城市污水污泥的热解还含有多环芳烃(多环芳烃)、萜烯,类固醇,单芳化合物,没有检测到这个工作。

可以看出热解生物油是复杂的混合物约46暂时鉴定有机化合物。在这种情况下,数额可观的氮氧化物芳香和环烃化合物存在于由于蛋白质和核酸的事实存在于原污水污泥。类似的化合物被确定,污水污泥的热解氮含量高(Dominguez et al.,2003,2005;Fullana et al.,2005)。所显示Fullana et al .(2003),芳香化合物可以形成两种可能的方式:脱氢氨基酸群存在于蛋白质和核酸,和氰化氢(HCN)和/或氨(NH3)单芳碳氢化合物(即苯和甲苯)在主要分解形成的。因此,之间的相似性可以发现在目前的研究结果和形成通路被Full-ana et al.(2003)。

果糖制造厂污水污泥的热解生物油(污泥X),最高的五个化合物的内容是:4-甲基苯酚(8.90%)、吡啶(3.38%)、2 -甲基吡咯(3.19%)、2 -甲基吡啶(2.95%),和2 -甲基吡嗪(2.56%)。相比之下,最高的五个化合物含量牛奶衍生物污水污泥的热解生物油(污泥Y)如下:棕榈酸(3.69%)、1H-吲哚(3.31%),十七酸(2.99%)、1-(1H-吡咯-2 -基)-乙酮(2.66%),和4-甲基-丙酮(2.66%);和1 -(1H-吡咯-2 -基)-乙-环己酮(3.11%)、吡啶(2.75%),2,6 -二甲基吡嗪(2.09%)、2 -甲基吡啶(1.62%),和2 -甲基吡咯(1.40%)

在啤酒制造污泥的热解生物油(SludgeZ)。应该注意,污泥的热解生物油高饱和脂肪酸(即的内容。,C15:0 C14:0 C16:0、C17:0 C18:0),结果表明,这些化合物应该直接来源于残留在污水污泥。然而,生物油污泥Y和Z显示非常低的污泥浓度的饱和脂肪酸。

表 1 显示了氮化作用的化合物,绝大多数都是氰基化合物和杂环。大多是结果根据获得的Fullana et al. (2003)和Zhai et al. (2008).。另一方面,确定的化合物可以是进一步分为以下类:

1 酚类化合物:4 - 甲基-酚和酚。

2 含氮芳香/杂芳香族化合物:吡啶,吡嗪,吡咯,嘧啶,吡啶-2-偕胺肟,1-氧化物喹喔啉,1H-吲

哚等,等等。

3 胺类:

4 -甲氧基苯胺。

4 酮类:1-(2-呋喃基)乙酮和2-羟基-2,4,6 -环庚三烯-1 -酮。

5 腈类:2-吡啶甲腈,苯乙腈,苯丙。

6脂肪族化合物:1-烯烃,含碳数范从C12到C19的烷烃和环烷烃。

7饱和脂肪酸:十二烷酸,十四烷酸,十五烷酸,十六烷酸,十七烷酸,并十八烷酸。

8 单芳族烃类:甲苯。

3.2 热解气体中不可冷凝的的成分

在前面的研究(Tsai et al.,2007),,排出气的成分从稻壳热解还包含一个相对少量的可压缩的有机化合物(即芳烃)。热解产物的研究结果解释了为什么总收益(包括液体和字符)在62-88%得到热解条件。确定的组成化合物在排出气感应加热高温裂解食品加工污水污泥,并用气相色谱-质谱法进行了半定量的分析基于面积的百分比抽搐的峰值。在所有情况下,只有25-35%的总色谱图ic面积被发现可能是因为许多化合物如多环芳烃(多环芳烃)、萜烯,醇类,酯类,这个工作没有检测到单芳族化合物。如上所述,数据报告的相对分布用于比较。表2显示了化合物的相对比例的值确定在这工作。生物油的三个食品加工污水污泥热解,较高的化合物内容如下:苯酚(2.4-3.7%),4-甲基苯酚(3.8-8.9%),1 H-吲哚(3.2-5.3%)、2 -甲基-1H-吲哚(2.5-3.0%)、棕榈酸(2.0-5.0%)、硬脂酸(-3.0%-1.8),和十六烷(2.0-3.2%)。当一个对比表1和表2的结果,这也是值得注意的一些化合物,包括2-乙基苯酚、2-甲基1H-吲哚,12-烷基十四酸,十六烷,明显发现在排出气,但没有确定裂解生物油。

表1

a生物污泥X,Y和Z分别取自果糖制造工厂,牛奶制造工厂,啤酒酿造工厂。热解液体产品获得300℃/min的升温速率和热解温度500℃。

b保留时间

3.3 气体产品的组成

包含从热解碳的气体产物组成的污水处理的污泥往往是富含CO、CO2和其他C1-C2脂肪族碳氢化合物(Dominguez et al.,2005,2006;Fullana et al.,2003;Karayildirim et al.,2006)。实验部分中提到,填充的柱用于有效地分隔的永久气体(即,N2,O2,CO和CO2)和C1-C2烃类(即CH4、C2H2、C2H4和C2H6)在这项工作。表3中所示是来自感应加热的气态产物的组成食品加工污水污泥的热解。表3中的数据相关C1-C2烃主要是甲烷,尤其是果糖制造污水污泥(污泥X)。相反,二氧化碳的浓度(即13025ppm)污泥X(即,分别为35687和26259 ppm)污泥污泥Y和Z。大多数不凝气体产

品已知的吸热气化反应热的有机原料和氧气不足条件(Dominguez et al .,2006):

能形成的水煤气变换反应:

甲烷和二氧化碳的浓度之间的变化可能是由于这样的事实,另一个放热反应是有利的:

表2

试探性的气相色谱-质谱表征非冷凝气体产品从食品加工污水污泥感应加热热解。

A 生物污泥X,Y和Z取自果糖制造工厂,牛奶制造工厂,分别和啤酒酿造工厂。热解液体产品获得300 C /min的升温速率和热解温度500 C。

B保留时间。

表3

成分的气体产品感应加热食品加工污水污泥的热解。

然而,进一步对H2的分析研究,将有助于阐明六氯环己烷和NH3的热解气体产品中的所有种在生物油中的热解产品鉴定信息机制和排气。

4.结论

在这项研究从食品加工工厂的三个污水厂污泥被重用作为诱导的喂料加热热解系统。热解生物油和排气气用气相色谱——质谱分析表明他们组成杂环化合物酚类物质,和组成的氮化作用芳香,脂肪羧酸中蛋白质和核酸是本原的污水污泥中的事实是合理的。在另一方面,转折的成分气体和轻烃的排气气体主要是二氧化碳、一氧化碳和甲烷。

致谢

该研究是由国科会(行政院国家科学委员会,台湾)根据合同编号NSC94-2211-E-041-021和国科会95-2221-E-020-040。

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Basic Control Actions and Industrial Automatic Control An automatic controller compares the actual value of the plant output with the desired value, determines the deviation, and produces a control signal which will reduce the deviation to zero or to a small value.The manner in which the automatic conroller produces the control signal is called the control action. Classifications of industrial automatic controllers Induetrial automatic controllers may be classified according to their control action as: ·two-position or on-off controllers; ·proportional controllers; ·integral controllers; ·proportional-plus-integral controllers; ·proportional-plus-derivative controllers; ·proportional-plus-derivative-plus-integral controllers. Most industrial automatic controllers use eletricity or pressurized fluid such as oil or air as power sources. Automatic controllers may also be classified according to the kind of power employed in the operation, such as pneumatic controllers, hydraulic controllers, or electronic controllers.What kind of controller to use must be decided by the nature of the plant and the operating conditions,including such considerations as safety, availability, reliability, accuracy, weight, and size? Elements of industrial automatic controllers An automatic controller must detect the actuating error signal, which is usually at a very low power level, and amplify it to a sufficiently high level. Thus, an amplifier is necessary. The output of an automatic controller is fed to a power device, such as a pneumatic motor or valve, a hydraulic motor, or an electric motor. The controller usually consists of an error detector and amplifier. The measuring element is a device that converts the output variable into another suitable variable, such as a displacement, pressure, or electric signal, which can be used for comparing the output to the reference input signal. This element is in the feedback path of the closed-loop system. The set point of the controller must be converted to a reference input of the same units as the feedback signal from the measuring element. The amplifier amplifies the power of the actuating error signal, which in turn operates the actuator. The actuator is an element which alters the input to the plant according to the control signal so that the feedback signal may be brought into correspondence with the reference input signal. Self-operated controllers In most industrial automatic controllers, separate units are used for the measuring element and for the actuator. In a very simple one, however, such as a self-operated controller, these elements are assembled in one unit. Self-operated controllers utilize power developed by the measuring element and are very simple and inexpensive. The set point is determined by the adjustment of the spring force. The controlled pressure is measured by the diaphragm. The actuating error signal is the net force acting on the diaphragm. Its position determines the valve opening. The operation of self-operated controller is as follows: Suppose that the output pressure is lower than the reference pressure, as determined by the set point. Then the downward spring force is greater than the upward pressure force, resulting in a downward movement of the diaphragm. This increases the flow rate and raises the output pressure.

英文翻译原文

Engineering with Computers(2002)18:109–115 Ownership and Copyright ?2002Springer-Verlag London Limited Structural Optimization of Automotive Body Components Based on Parametric Solid Modeling M.E.Botkin GM R&D Center,Warren,MI,USA Abstract Abstract::Parametric modeling was used to build several models of an automotive front structure concept that utilizes carbon fiber composite materials and the corresponding molding processes.An ultra-lightweight aluminum body front structure was redesigned to include an all-composite front structure.Two alternative concepts were studied which represent the structure as a bonded assembly of shells.Closed sections result from two pieces–an inner and outer.Parametric modeling was found to be a useful tool for building and modifying models to use in optimization concept studies. Such models can be built quickly and both the sketch dimensions and location dimensions are particularly useful for making the adjustments necessary to fit the various body pieces together.The parametric models then must be joined together as one geometric solid model in order to obtain a surface mesh.Structural optimization input data can then be seamlessly and quickly created from the parametric-modelbased finite element model to begin the tradeoff studies.This integrated process in which parametric modeling was coupled with structural optimization was used to carry out design studies on the lightweight body front structure.Several carbon fiber material combinations were studied to determine mass reduction potential of certain types of carbon fiber products considered to be lower cost than typical carbon fiber materials used in the past.Structural optimization was used to compare several composite constructions for the design of the bonded front structure.Eight cases were studied using various materials and composite lay-ups.Mass savings estimates from45–64%over steel were obtained.The most reasonable design consisted of a combination of relatively low cost chopped carbon fiber and woven carbon fiber and using a20mm balsa core in the top of the shock tower area. This design had a maximum thickness of7mm and a mass reduction over steel of approximately62%.Correspondence and offprint requests to:Mark E.Botkin,Principal

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