含油污泥热解工艺优化及资源化利用

针对含油污泥危害性大、难处理的环保难题,以实现含油污泥资源化利用为目标,开展了含油污泥热解实验研究,优化了热解工艺,并对热解产物进行了分析。在催化剂加量1.2％、热解温度为420℃、停留时间3.0 h、加热速率12℃/min、N2流速为90 mL/min条件下对含油污泥进行热解,结果表明：热解油回收率 可达72.35％;热解回收油品质有较大的改善,产生的不凝气体组分可用于燃烧供热,热解残渣热值较高,可制成燃料重复利用,实现了含油污泥的资源化利用。     

热解装置对含油污泥热解产物的影响

以含油污泥为研究对象,采用三种不同的热解装置(20g格金试验干馏炉,20kg固定床及2 000kg/h神雾无热载体蓄热式旋转床,简称"旋转床"),探讨热解装置的差异对含油污泥热解产物产率和性质的影响。结果表明,与其他两种热解装置相比,旋转床中热解气和热解液产率最高,分别为27.34%和37.19%,但与固定床差异不显著,且热解气热值最高(20.08 MJ/m3),旋转床热解液中热解油的轻质组分含量以及热值最高,分别90.75%和48.01MJ/kg。格金装置中热解固体产率显著高于其他两种装置,且固体中灰分含量最低。因此,旋转床用于含油污泥热解处理工艺,不仅可以最大程度地减少固体残渣的产生,还可获得较高产率和品质的可燃气和热解油,对含油污泥的减量化和资源化效果显著。     

油田含油污泥与芦苇共热解实验研究

以北方某油田湿地芦苇与油田某污水处理厂剩余污泥为对象,利用同步热分析仪及静态热解炉研究油田含油污泥及含油污泥-芦苇混合物的热解特性,将静态热解过程数据与同步热分析TG(热重分析)、DTG(微分热重分析)、DSC(差示扫描量热分析)曲线结合,计算了终止温度、产物量等。结果表明:不同含油污泥样品其产物生成率差别不大,热解TG、DTG和DSC曲线有较大差别,添加一定比例的芦苇可以使含油污泥热解过程变得匀速缓和,5%(质量比)的芦苇添加量可以使热解残渣恒重温度降低约25℃。混掺芦苇的样品残渣呈分散颗粒状,无聚结现象,对热解结焦将产生一定抑制作用。     

生物质在固定床中的热解试验研究

介绍了用于生物质热解的试验装置及试验方法，研究了升温速率、热解温度两种关键因素对生物质热解产物得率及其分桕的影响。研究结果表明，随热解温度的升高，热解产气量增加，且其中气体产品中的有效成分也在增加，焦油和半焦减少；升温速率增加，热解气得率增加，且气体中有效可燃成分增加。     

CO变换反应与煤热解耦合反应特性研究

本文在上层为变换催化剂B113下层为新疆伊犁南台子煤粒的固定床反应器中,研究CO变换反应与煤热解的耦合作用。考察了CO变换反应水气比、煤热解温度对耦合反应的影响,研究了耦合热解所得各项产物的特性。结果表明,水气比为1.0、热解反应温度为650℃时耦合热解获得最高的焦油产量,焦油产率为16.36%,比氮气气氛下的焦油产率增加了6.66个百分点,比氢气气氛下增加了4.49个百分点;耦合热解可以得到更低硫的半焦,在终态温度为750℃时耦合热解脱硫率为92.28%;热解气体产物中氢气、甲烷、C2-C4烃类气体含量增加;焦油的羟基数量减少,脂肪烃和芳香烃增多。     

含油污泥热解处理的试验与应用

介绍了欢三联含油污泥热解处理工程的工艺流程、技术要点、设计参数、运行效果和效益情况。调试工作表明,热解炉系统工艺作为一个整体,能够稳定有效运行,残渣的测验结果表明,残渣可以达到无害化程度,含油率小于0.3%(满足GB 4284-84《农用污泥中污染物控制标准》的要求)。以12t/d的处理量运行,能耗成本为74.47元/t,产生的经济效益为125.50元/t,同时产生较好的社会效益。另外,热解固态产物也有较好的利用价值,可以进一步研究利用。     

含油污泥热解工艺技术方案研究

文章以辽河油田欢三联合站稠油污水处理系统压滤脱水污泥及沉降罐清罐污泥为处理对象,根据含油污泥热解处理的技术原理,通过对物料输送系统、热解反应系统、剩余固体排出系统和馏分冷凝分离系统等主要工艺单元的技术比选,提出了"柱塞泵管道密闭输送、多燃烧器回转炉热解、高温馏分管式换热器冷凝、不凝气罗茨风机引送和湿式排渣"的含油污泥热解处理工艺技术方案。同时,文章还对污泥热解处理运行的能耗与费用做了简要理论分析。     

油基岩屑热解后剩余固相资源化利用研究

热解剩余固相作为油基岩屑的无害化处理产物，其资源化利用方式受到广泛关注。文章分析了剩余固相的性质与组成，重金属含量低于GB 15618—2018《土壤环境质量 农用地土壤污染风险管控标准（试行）》管制值，存在资源化利用的可能性。基于近年来的研究成果，综述了剩余固相在制水泥、砖、路基材料方面 的资源化利用途径，剩余固相中的火山脂活性可以提供建材所需的力学性能。从机理方面分析了剩余固相作 为催化剂和吸附材料的优势，其中含有的过渡金属可以有效催化多种反应，且具有化学吸附作用。解读了国内 油基岩屑热解后剩余固相资源化利用方面的最新政策，对以后的研究方向进行了展望。     

污水污泥低温催化热解实验研究

在实验室研究了不同热解温度下,经污泥低温热解残留物催化作用,污泥低温催化热解产物的产率及特性。结果表明,与无催化剂相比,污泥低温热解所得的液体产率、油品产率、气体产率等明显增加。油品最大产率所需温度从440℃降低至400℃,油品最大产率从20.5%增加到24.5%,油品的品质有一定的提高。     

生物质热解影响因素研究

阐述了生物质的特点及其热解的定义和热解机理,综述了生物质热解过程中,温度、升温速率、物料特性（如种类、分子结构、粒径和颗粒形状等）、滞留时间、压力等操作条件对生物质热解及其产物分布组成和特性的影响,指出了生物质热解的技术关键。     

Pyrolysis of commingled waste textile fibers in a batch reactor: Analysis of the pyrolysis gases and solid product

The main object of this study was the investigation of the thermal recycling of commingled waste textile fibers, with the aim of the production of useful end products. Differential scanning calorimetry/Thermo gravimetric analysis (DSC/TGA) was applied to determine the thermal degradation characteristics of the commingled waste textile fibers and there are two peaks located at the temperature ranges of 299–360°C and 399–500°C. Commingled waste fiber was pyrolyzed in a nitrogen atmosphere in relation to three different temperatures (500, 600, and 700°C), heating rates (25 and 50°C min^?1), and retention times (15 and 30 min). The effect of the experimental conditions such as pyrolysis temperature, heating rates, and retention time on the formation of char and gas--liquid products was investigated and the product yields were determined from the rate of the weight loss. The highest conversion rate 82.9 wt.% liquid--gas product and 17.1 wt.% char product was achieved at 700°C. Pyrolysis gases were taken for every 7, 15, and 25 min and were analyzed for major components such as CO, CO₂, CH₄, and H₂ by gas chromatography. The pyrolysis char called as carbon black derived from the pyrolysis of commingled waste textile fibers was analyzed for a range of properties, including the elemental analysis, moisture content, ash content, calorific value, and trace metal analysis.     

Characterization of fuel gas products from the treatment of solid waste streams with a plasma arc torch

This work addresses the plasma treatment of two solid waste streams and production of fuel gases from the process. In this study, carpet waste and simulated solid wastes generated by a United States Air Force Basic Expeditionary Airfield Resources Base deployment were used. Waste was treated in a furnace fitted with a 100kW plasma arc torch. The off gas was analyzed to determine its composition. The product gas was composed primarily of carbon monoxide and hydrogen, with small amounts of methane, benzene and toluene also detected. These experiments demonstrate the feasibility of producing fuel gases by plasma treatment of the solid waste streams. While the thermal energy value of the fuel gas produced in these experiments was less than the energy input, a higher waste-to-fuel gas conversion efficiency is expected in full-scale application.     

Rubber tire life cycle assessment and the effect of reducing carbon footprint by replacing carbon black with graphene

This research utilizes real operating data from a tire plant operating in Central Taiwan to investigate the carbon footprint emissions (CO₂e) involved in producing the electric bicycle. The simulation results are based on the PAS 2050 standard using the SimaPro 7.3 software tool. Our results show the total carbon footprint emissions of 1.2-kg tire for the electric bicycle weighing 4.53-kg CO₂e, composed of 2.63-kg CO₂e from raw tire materials stage, 1.295-kg CO₂e from tire manufacturing stage, and 0.605-kg CO₂e from tire transport stage. An international certified organization, British Standard Institute (BSI), verified the accuracy of our results as 98.7%. We found that carbon emissions at the raw materials stage were higher than that for the other two stages – manufacturing and transportation. Carbon black was determined as the maximum source of carbon emissions at the raw material stage. To reduce the tire plant carbon emissions, this paper recommends using graphene to replace carbon black. Graphene has been reported by many researches to improve the properties of rubber products. From our simulation results, the carbon footprint emissions of 4.56-kg CO₂e of the origin tire plant uses 0.456-kg carbon black to produce 1.2-kg electric bicycle tires. This can be reduced to 4.29 (5.92%), 4.03 (11.62%), 3.75 (11.76%), and 3.49-kg CO₂e (23.46%) by using graphene to replace carbon black 25, 50, 75, and 100 wt% respectively. If we focus only on 0.456-kg carbon black producing 1.08-kg CO₂e, the reduced carbon footprint will be 0.812 (24.81%), 0.547 (49.35%), 0.28 (74.07%), and 0.0128-kg CO₂e (98.81%) by using graphene to replace carbon black 25, 50, 75, and 100 wt% respectively. From our analysis, graphene replacing carbon black can reduce carbon footprint. This has not been published previously and provides a direction for the tire plant to save carbon emissions.     

Conversion of leather wastes to useful products

The main objective of the present study is to investigate the production of useful materials from different kinds of leather waste. Three different types of tannery wastes (chromium- and vegetable-tanned shavings, and buffing dust) were pyrolyzed in a fixed bed reactor at temperatures of 450 and 600 °C under N₂ atmosphere. Gas, oil, ammonium carbonate and carboneous residue were obtained by pyrolysis. The effect of temperature and type of leather waste on product distribution of pyrolysis was investigated. Buffing dust gave the highest yield of oil (ca. 23%), while other wastes recorded yields of ca. 9%. Results of elemental analysis and column chromatography showed that pyrolysis oils could be used as fuel or chemical feedstock after re-treatment. The yields of carboneous residue (chars) were between 37.5% and 48.5% and their calorific value was between 4300 and 6000 kcal kg⁻¹, suitable for use as solid fuel. In addition, these chars were activated by CO₂ to obtain the activated carbon. The activated carbon having highest surface area (799.5 m² g⁻¹) was obtained from chromium-tanned shavings. Activated carbons prepared from chromium-tanned leather were presented as an adsorbant for the adsorption of dyes from aqueous solution.     

Recyling of plastic wastes via pyrolysis

Pyrolysis for the simultaneous generation of oils and gases can be convenient to obtain hydrocarbons and even to recover crude petrochemicals or to generate energy from waste plastics. A Gray–King apparatus has been used to pyrolyze waste polyethylene (PE), polystyrene (PS), both separately and with different compositions. Thermogravimetric analysis of waste plastics indicated the critical temperatures, which should be effective for pyrolysis. The chosen heating rate was low in order to achieve higher liquid yields. The results showed that waste PS yielded higher liquid, and waste PE yielded higher gaseous products. The dominant liquid product of PS waste was styrene whereas for waste PE, prophenylbenzene was the dominant pyrolysis product.     

改造碳黑废水处理设施使废水循环使用

介绍碳黑废水处理工艺流程的技术改造及其技术要点。着重阐述了关键设备斜管沉淀池的运行原理、运行结果及其在整个流程改造过程中所起的作用。改造后的工艺流程特点是斜管沉淀效率高，出水水质好，副产品碳黑质优销路好，劳动强度低，废水可循环使用，设备占地少，运行费用低，总体效益好。改造后实现了全厂生产用水闭路循环，取得了可观的经济、环境、社会效益。废水循环利用在技术上是可行的，经济上有收益，实现了废水及固体废物的资源化。     

含油污泥的热解处理与利用

文章对油田和炼油含油污泥进行了热解处理室内实验,测定了回收油气组成、热解残渣含碳量和Al2O3含量,开展了热解残渣对沥青的吸附性能和再生处理的絮凝性能测试分析。结果表明,含油污泥热解处理具有较好的油气回收和残渣再生利用价值,可实现污泥“零排放”,具有显著的直接经济效益和社会效益。污泥热解的产油率一般可达10%以上,废白土可达20%～30%,油回收率高;污水处理污泥热解残渣的Al2O3含量可达20%以上,有较高的铝含量,初步再生评价对污水有较好的絮凝作用,可再生循环利用;废白土热解残渣的吸附性能与活性白土相当,可循环使用。     

橡胶制品工业工艺废气排放因子探讨——以轮胎企业为例

介绍AP-42、GB27632—2011中橡胶制品工艺废气污染物情况,并与轮胎企业工艺废气污染物实测数据进行比较分析,探讨了工艺废气的排放因子。结果表明轮胎企业工艺废气主要来自于炼胶、硫化工序,排放主要污染物为颗粒物、二甲苯、非甲烷总烃和二硫化碳,排放因子可参照AP-42确定。     

含油污泥热解残渣吸附性能初探＊

含油污泥热解残渣的处理和应用是石油石化企业生产领域急需解决的难题。以含油污泥热解残渣为研究对象,在对其进行无害化处理的基础上,对热解残渣的吸附性能进行了探讨。通过能谱分析可知,热解残渣由碳和无机元素组成,碳元素含量达36.92%;通过SEM电镜扫描、比表面积和孔结构等吸附性质表征研究,含油污泥热解残渣吸附性能优良,对含油污水中的石油类和COD有较好的去除作用。研究结果表明:含油污泥热解残渣可作为一种吸附材料,这项研究为含油污泥热解残渣的资源化利用提供了一条途径。