化学键合吸附剂的合成及吸附行为

在无定型硅胶上化学键合十八烷基三氯硅烷，键合率17%-20％，粒度5μm-10μm，以此键合的吸附剂可有效地吸附香烟烟气中的焦油、亚硝胺，吸附率分别为15%-18％和37%-43％，研究了化学键合吸附剂的粒度和加入量对吸附性能的影响。     

On the rank-dependence of coal tar secondary reactions

The secondary reactions of volatile compounds, including coal tar and light gases, accounts for a great portion of soot formation and the subsequent heat release and pollutant emissions in the combustion zone. While coal primary pyrolysis has been extensively studied over the last few decades and several network pyrolysis models has been developed to describe this process, coal secondary pyrolysis is still not well understood. The Babcock and Wilcox Company has been investigating coal secondary pyrolysis in order to develop a comprehensive mechanism for inclusion in predictive computational fluid dynamics and coal combustion models. Supportive experiments were carried out in an entrained-flow reactor. Tar was extracted from the pyrolysis byproducts of seven coals of widely-distributed rank at temperatures ranging from 923 to 1473 K, and analyzed by ¹³C NMR. Tars formed from higher rank coals generally demonstrated higher sooting propensities. This rank-dependent sooting propensity is associated with tar’s chemical structure properties. With increased heat treatment severity, tar molecules lose a substantial amount of aliphatic attachments, and the average size of substitution per cluster decreases. Compared to tars formed from high-rank bituminous coals, those formed from low-rank sub-bituminous coals have a larger attachment portion, higher averaged substitution, and higher oxygen-containing functional groups. These differences contribute to the higher cracking propensity observed for low-rank coal tars.     

Gasification characteristics of woody biomass in the packed bed reactor

Gasification technology is recognized as one of the possibilities for utilizing biomass effectively. This study focused on woody biomass gasification fundamentals, using a bench-scale packed-bed reactor. In this experiment, pellets of black pine were gasified, using air as the oxidizing agent. Gasification tests were carried out under both updraft and downdraft conditions. Temperature distributions and compositions of syngas inside the gasifier were continuously monitored during gasification experiments at several ports on the wall of the reactor. The syngas at the exit of the gasifier was also sampled to estimate the amount of tar. Lower heating values of the syngas under updraft and downdraft conditions were 4.8 and 3.8 MJ/m³N, respectively. It was easier to control the height of the packed bed under the downdraft condition than under the updraft condition. Under the updraft condition, a bridging phenomenon occurred. Tar generation under the downdraft condition was lower than that under the updraft condition. This is because tar passes through a partial combustion zone or higher temperature zone in the downdraft gasifier.     

Kinetic study for liquefaction of tar in sub- and supercritical water

Liquefaction of tar from oil distillation was studied under sub- and supercritical water conditions using a batch reactor at 623 and 673 K and 25-40 MPa. The reaction scheme for tar liquefaction was determined as follows: the liquefaction process of tar occurs first and then intermediate chemical compounds are transformed into lighter molecular weight species. The effects of pressure and treatment time were combined into a single severity parameter that was used to monitor the conversion of tar. The main products from the liquefaction of tar were phenol (3.44 wt%), biphenyl (2.23 wt%), diphenylether (13.70 wt%) and diphenylmethane (1.30 wt%), respectively. Liquefaction of tar clearly increased with increasing water density at the same temperature reaction. It indicates that hydrolysis was important in the cleavage of the macromolecular structure of tar under sub- and supercritical conditions. Based on the results, this method could become an efficient method for tar liquefaction, producing high yields of valuable chemical intermediates.     

Predicting nitrogen release during coal tar decomposition

This paper develops a detailed phenomenological reaction mechanism for N-species transformations throughout tar decomposition, including tar-N sequestration into soot. It expands the previously validated mechanism for tar decomposition based on FLASHCHAIN^® theory to cover N-transformations during pulverized fuel firing. Tar-N transformations are described by two distinctive features: (1) An elimination reaction that produces HCN governs the decay in the average moles of nitrogen per aromatic nucleus throughout tar decomposition; and (2) Empirical observations determine the fraction of tar-N incorporated into soot. Validation cases represent heating rates of at least several thousand degrees per second; temperatures from 600 to 1100 °C; tar contact times from 75?ms through 2?s; and coal ranks from subbituminous through low volatile bituminous. The predicted partitioning of coal-N into tar-N, HCN, soot-N, and char-N was within measurement uncertainties for all coals for simulated p. f. firing conditions, including the variation in fractional char-N levels from 0.4 to 0.8 across this domain. Since primary tar-N levels are directly proportional to fractional primary tar yields, and since ultimate soot-N levels account for one-third of tar-N with any coal type, the ultimate coal-N partitioning for CFD furnace simulations can be accurately described with two analyses: (1) A primary devolatilization mechanism to predict primary tar yields under rapid heating conditions; and (2) A submechanism to predict HCN release from char throughout devolatilization up to the point of char ignition. Dynamics may be resolved with either global reactions or the full tar decomposition mechanism, depending on the impact of the lag between tar decomposition and soot production in the subject application.     

Characterization of coal tars by HPLC group type separation and capillary GC of volatiles

Summary Group separation of malthene fractions of tar samples obtained from brown coals of different ranks at two different temperatures (500 and 800°C) was performed by HPLC using amino-cyano bonded phase packing with two eluent systems of different polarities and backflushing technique. Group composition of different tar samples was compared and evaluated. Amount and distribution of volatile compounds in the malthene fractions were determined by capillary gas chromatography on a CP-Sil 5 WCOT column. Presented at the 15th International Symposium on Chromatography, Nürnberg, October 1984     

Comparative study of crude oils from the Machete area in the Eastern Venezuelan Basin by pyrolysis of asphaltenes

This work is an analysis of crude oil samples from the two most recent producing wells in the Machete area (Orinoco Tar Belt, Venezuela). The aim is to determine the type of environment in which the precursor organic materials were deposited. In spite of the fact that the degree of maturity and the biodegradation of the two crude oils are similar, their characterization leads us to conclude that they have very distinctive and different origins. The comparative study was performed by separating their main fractions, pyrolysis of asphaltenes, and further identification of several indicators (aromatic, polar and sulfur compounds, linear aliphatic hydrocarbons, and cadalene). Moreover, several biomarkers (terpanes, hopanoids and steranes) present in the saturated fractions obtained from the two crude oils were analyzed by using gas chromatography combined with mass spectrometry (GC–MS). The statistical study of geochemical indicator values and relative proportions of lipid and lipid-like biomarkers present in products from asphaltene pyrolysis shows a high probability of there being two distinct crude oil families from the Machete area.     

几种吸附材料去除主流烟气中的挥发性醛酮类化合物

研究了分别添加活性炭、竹炭、海泡石、壳聚糖的卷烟复合滤咀对主流烟气中挥发性醛酮类化合物和其他有害物质(如焦油、一氧化碳等)的吸附效果.研究结果表明:壳聚糖滤嘴的吸附性能大干活性炭,竹炭和海泡石;活性炭的吸附性能优于竹炭和海泡石.对于焦油,海泡石的吸附作用最大,竹炭、活性炭有一定的吸附,壳聚糖则无明显影响.壳聚糖对于烟气...     

Ni/MgO-Al2O3催化剂上高温焦油组分的催化转化

采用分步浸渍法制备了MgO-Al2O3负载的Ni基催化剂, 并运用N2吸附、载射线衍射(XRD)、透射电子显微镜(TEM)等手段进行表征. 该催化剂用于甲苯或萘为焦油模拟化合物的高温焦炉煤气(COG)的常压加氢裂解反应, 并考察了H2浓度、H2S对催化剂活性的影响. 结果表明: 催化剂还原后, 表面形成均匀分散、直径为8-14 nm的金属Ni纳米颗粒; 在较低的水碳摩尔比(nH2O/nC=0.28)时, 甲苯就能完全转化并选择性地加氢裂解形成CH4, 测试的时间内(480 min), 催化剂没有明显的失活和积炭现象, 显示出好的反应活性、稳定性和耐硫能力. 制得的Ni/MgO-Al2O3催化剂有望应用于较低水含量(10%-15%(φ, 体积分数))的高温焦炉煤气中焦油的直接转化.     

液化残渣的微波热解与常规热解对比分析

采用微波加热和常规电加热两种条件进行液化残渣(DCLR)的热解实验,考察了热解产物固体焦、焦油及煤气的组成及结构的变化规律,采用红外分析(FTIR)与气相色谱-质谱(GC-MS)联用技术对热解产品进行了分析表征。研究表明,在微波场中,DCLR的升温速率很快,20 min左右物料温度就可达到900 ℃,最大升温速率可达到329 ℃·min-1,而常规加热的升温速率基本保持恒定。与常规热解相比,微波热解后固体焦的产率降低2.85%,而焦油和煤气产率分别增加了0.66%和2.19%。DCLR热解后固体焦的索氏萃取组分重油(HS)、沥青烯(A)及前沥青烯(PA)含量均大幅降低,而四氢呋喃不溶物(THFIS)则有所增加,但是两种热解条件下得到的固体焦的四种索氏组成差异不是很大,说明DCLR的热解过程是以HS,A与PA的转化为主的。微波热解后固体焦红外谱上3 437.6,1 632.0 cm-1以及1 079.99 cm-1处吸收峰的强度与常规热解相比明显降低,说明微波场中DCLR的热解更为彻底。热解后焦油和煤气产率均有所增加,煤气中H₂含量均达到60%以上。GC-MS分析表明,经由石油醚萃取后的热解焦油中脂肪类、芳香类与醇类物质组成以及C_1~5,C_11~20与C₂₀以上组分的含量均没有发生明显变化,而微波热解焦油中沥青质的含量则下降了7.7%,说明微波作用可有效促进DCLR中沥青质的热分解,有利于热解焦油的轻质化。