废旧电路板元器件解锡技术研究

废旧电路板上元器件与线路板的解锡脱离是电路板资源化的关键。分析了国内外手工、机械、加热和化学4种解锡技术的发展,对可行的加热解锡和机械拆卸组合的工艺技术进行研究分析,提出了废旧电路板元器件解锡技术的研究方向和重点。     

面向经济回收的产品设计系统构成

面向回收的产品设计能够使废旧产品得到更好的回收和重用 , 优化拆卸序列的生成必须基于产品拆卸的经济性分析 . 论述了面向经济回收的产品设计系统的构成及相关的关键问题 , 分析了产品的零件材料回收价值与拆卸工艺 , 建立了零件材料合理回收的评估方法 .     

报废电冰箱的环保处理技术

介绍一种处理报废电冰箱的技术。首先对报废电冰箱进行分解,包括制冷剂回收、压缩机拆卸、散热系统和蒸发系统拆卸、箱体箱门钢板拆卸、箱体内胆拆卸、门衬拆卸和绝热泡沫剥离等。然后对于拆出的材料作进一步处理,钢板、管材经平整或矫直裁剪之后作为旧板材或旧管材;内胆和门衬破碎后作为注塑材料使用;压缩机组经专业检测、修复再利用或作为冶金炉料使用。聚氨酯泡沫需经分离回收R11处理,处理工艺路线包括泡沫粉碎、发泡剂蒸发、混合气收集、除尘、储气、压缩、冷凝、节流以及发泡剂与空气的分离;工艺参数涉及主要工艺环节的热力学计算,包括破碎后的泡沫中的R11发泡剂的蒸发吸热、混合气压缩功耗、冷凝过程的散热。同时还介绍了应用发泡胶接法的聚氨酯硬泡沫碎屑再成型技术。采用该工艺处理报废电冰箱,具有拆解物利用价值高、处理过程能耗低、便于分拣、设备造价低等优点,适合我国国情。     

一种废电脑CPU的分离回收方法

<正>专利申请号:CN201811218111公开号:CN109389230A申请日:2018.10.19公开日:2019.02.26申请人:长沙汇聚环境技术有限公司;本发明提供了一种废电脑CPU的分离回收方法,首先从废旧电脑主板上拆除废旧CPU,将针脚和CPU基座分离;将针脚与钢球、介质油混合,加入立式搅拌球磨机中,球磨将针脚表层的金镀层和少量的铜从铜质针脚上剥离,筛分得到脱除     

工信部基础电子元器件产业发展行动计划(2021—2023年):绿色制造提升行动

建设绿色工厂.按照厂房集约化、原料无害化、生产洁净化、废物资源化、能源低碳化原则引导电子元器件企业建设绿色工厂,加大节能环保投入,实施节能环保技术提升工程,鼓励企业采用信息化、智能化技术处理污染物并实时监控,将企业的环保执行措施与企业信用等级挂钩.生产绿色产品.严格执行《电器电子产品有害物质限制使用管理办法》等政策,鼓...     

专利资讯

<正>专利名称:一种离心废旧电路板原件拆卸机专利申请号:CN201420308822.1公开号:CN203853642U申请日:2014.06.11公开日:2014.10.01申请人:任永斌一种离心废旧电路板原件拆卸机,由保温外壳、转子、电路板支架、电动机、电热丝组成,在保温外壳中有转子及电热丝,转子中含有电路板支架;采用了本实用新型的方案,克服现有废旧电路板原件拆卸机操作复杂、效率低的缺点,可以批量快速拆卸废旧电路板。     

国内外线路板电子元件去除及贵金属提取现状分析

围绕线路板的处置和资源化利用,介绍了国内外线路板电子元器件去除及贵金属提取现状,对现有回收方式的原理、效益和推广程度进行了阐述.     

从废印制电路板元器件中分离电容器的方法

以典型废印制电路板湿法剥离得到的元器件为研究对象,通过筛分和磁选相结合的物理方法,分离其中的电容器。研究发现,筛分后电容器分布在9.5-19 mm和4.0-9.5 mm范围内,并且50%以上的元器件与电容器得到分离。9.5-19 mm范围内的元器件经过磁选,可以将强磁性的铜线绕阻类元器件分离出来,剩余元器件采用8 mm宽的条形筛进行筛分,筛上物主要为电容器,筛下物主要为芯片和引脚;4.0-9.5 mm范围内的元器件经过磁选,可以将92.93%的电容器分离出来。     

电冰箱的回收处理及绿色设计探讨

冰箱产品从其制造到废弃是一个庞大的产业领域,如何以较经济的方式实现废旧冰箱的可拆卸性与可回收性以及冰箱的绿色设计已经成为当今国际社会关注的热点.针对废旧冰箱的拆卸与回收的经济性、再生程序以及绿色冰箱的设计等方面进行了分析.     

一种从废旧手机电路板中提取铜和金的方法

正专利申请号:CN201610496735.7公开号:CN106086417A申请日:2016.06.27公开日:2016.11.09申请人:南开大学本发明为一种从废旧手机电路板中提取铜和金的方法,属于资源循环领域。目前针对电路板中金属的提取主要对象是电脑主板,而针对手机电路板中金属的提取方法很少,本专利提供的方法可以解决这一问题。同时,针对以往硫脲法     

Determination of the Thermal Efficiency of Pre-boilover Burning of a Slick of Oil on Water

The burning rate of a slick of oil on a water bed is calculated by a simple expression derived from a one-dimensional heat conduction equation. Heat feedback from the flame to the surface is assumed to be a constant fraction of the total energy released by the combustion reaction. The constant fraction (χ) is named the burning efficiency and represents an important tool in assessing the potential of in situ burning as a counter-measure to an oil-spill. The total heat release, as a function of the pool diameter, is obtained from an existing correlation. It is assumed that radiative heat is absorbed close to the fuel surface, that conduction is the dominant mode of heat transfer in the liquid phase and that the fuel boiling temperature remains constant. By matching the characteristic thermal penetration length scale for the fuel/water system and an equivalent single layer system, a combined thermal diffusivity can be calculated and used to obtain an analytical solution for the burning rate. Theoretical expressions were correlated with crude oil and heating oil, for a number of pool diameters and initial fuel layer thickness. Experiments were also conducted with emulsified and weathered crude oil. The simple analytical expression describes well the effects of pool diameter and initial fuel layer thickness permitting a better observation of the effects of weathering, emulsification and net heat feedback to the fuel surface. Experiments showed that only a small fraction of the heat released by the flame is retained by the fuel layer and water bed (of the order of 1%). The effect of weathering on the burning rate decreases with the weathering period and that emulsification results in a linear decrease of the burning rate with water content.     

Review of the kinetics of alkaline degradation of cellulose in view of its relevance for safety assessment of radioactive waste repositories

The degradation of cellulose (a substantial component of low- and intermediate-level radioactive waste) under alkaline conditions occurs via two main processes: a peeling-off reaction and a basecatalyzed cleavage of glycosidic bonds (hydrolysis). Both processes show pseudo-first-order kinetics. At ambient temperature, the peeling-off process is the dominant degradation mechanism, resulting in the formation of mainly isosaccharinic acid. The degradation depends strongly on the degree of polymerization (DP) and on the number of reducing end groups present in cellulose. Beyond pH 12.5, the OH^- concentration has only a minor effect on the degradation rate. It was estimated that under repository conditions (alkaline environment, pH 13.3-12.5) about 10% of the cellulosic materials (average DP = 1000-2000) will degrade in the first stage (up to 10⁵ years) by the peeling-off reaction and will cause an ingrowth of isosaccharinic acid in the interstitial cement pore water. In the second stage (10⁵-10⁶ years), alkaline hydrolysis will control the further degradation of the cellulose. The potential role of microorganisms in the degradation of cellulose under alkaline conditions could not be evaluated. Proper assessment of the effect of cellulose degradation on the mobilization of radionuclides basically requires knowing the concentration of isosaccharinic acid in the pore water. This concentration, however, depends on several factors such as the stability of ISA under alkaline conditions, sorption of ISA on cement, formation of sparingly soluble ISA-salts, etc. A discussion of all the relevant processes involved, however, is far beyond the scope of the presented overview.     

Study of Aging Characteristics of Ternary Blends of Polyethylenes—II

Six film samples of low-density polypropylene (LDPE)/linear LDPE (LLDPE)/high-density polypropylene (HDPE) with varying ratios of LDPE (20–45 ... wt%) and LLDPE (25–50 wt%) having a fixed amount of HDPE at 30 wt% were prepared by blown film extrusion technique. The samples were aged at four different temperatures, 55°, 70°, 85°, and 100°C, for four different time periods in the interval of between 150 hours and up to 600 hours. The change in the structure of various constituents and the formation of various oxygenated (peroxy and hydroperoxy) and unsaturated groups during thermo-oxidative degradation was discussed by infrared spectroscopy. The visiosity-average molecular weight was found to have decreased slowly in the initial aging hours and temperatures, whereas it decreased by 10% with its previous value tensile strength that is, 100°C when aged for 600 hours. The tensile strength of the sample first increased by 67% at 55°C and 89% at 70°C up to 450 hours, whereas the values increased by 52.5% at 85°C and 33.9% at 100°C when aged for 150 hours and then decreased. The percentage elongation at break increased by 2.7% at 55°C and 10.7% at 70°C for 150 and 300 hours of aging, respectively, whereas the percentage decreased when aged at 85°C and 100°C for up to 600 hours of aging. The values of gel content (percent) increased and initial degradation temperature decreased with aging time and temperature.     

富拉尔基发电总厂200MW机组除尘器改造

对富拉尔基发电总厂5号炉的设计条件进行了分析，针对燃用低硫煤，飞灰比电阻高，场地较小，除尘效率要求高的情况，在电除尘器的设计上采取有效措施，达到了排放要求。     

Calculation of carbon balances for evaluation of the biodegradability of polymers

Establishing carbon balances has been proven to be an applicable and powerful tool in testing biodegradability of polymers. In controlled degradation tests at a 4-L scale with the model polymer poly(-hydroxybutyrate) (PHB), it was shown that the degree of degradation could not be determined with satisfactory accuracy from CO₂ release alone. Instead, the course of degradation was characterized by means of establishing carbon balances for the degradation of PHB withAcidovorax facilis and a mixed culture derived from compost. Different analytical methods for determining the different carbon fractions were adapted to the particular test conditions and compared. Quantitative determination of biomass and residual polymer were the main problems in establishing carbon balances. Amounts of biomass derived from protein measurements depend strongly on assumptions of the protein content of the biomass. Selective oxidation of biomass with hypochlorite was used as alternative, but here problems arose from insoluble metabolic products. Determination of soluble components with the method of chemical oxygen demand (COD) also includes empirical assumptions but seems acceptable if the dissolved carbon fraction is in the range of some 10% total carbon. Results confirm both analytical assays and theoretical approaches, in ending up at values very close to 100%, within an acceptable standard deviation range under test conditions comparable to standard test practice.Paper presented at the Bio/Environmentally Degradable Polymer Society—Third National Meeting, June 6–8, 1994, Boston, Massachusetts.     

Effects of temperature on the release of nutrient elements of solid organic materials under conditions of oversaturation

The effects of temperature on the release of chemical components of six solid organic materials under conditions of oversaturation were investigated in this paper. The six materials were peat moss (PM), weathered coals (WC), charred rice husks (CRH), sawdust (Sd), turfgrass clippings (TC), and chicken manure (CM). Significant differences were observed in the available nitrogen and phosphorus content of the aqueous extracts of organic materials at different temperatures. The available nitrogen content in aqueous extracts of PM and WC at 25 °C was higher than that registered at 15 °C and 35 °C. Available nitrogen content in the aqueous extracts of CRH, Sd, TC, and WC at 35 °C was higher than at 15 °C and 25 °C. The available phosphorus content in the aqueous extracts of organic materials at 35 °C was higher than that available at 15 °C and 25 °C, with the exception of Sd. In addition, the release of available phosphorus in the aqueous solution of organic materials at different temperatures varied constantly for 108 h. The release of potassium (K⁺) and sodium (Na⁺) ions in the aqueous extracts of organic materials was basically steady over time, with the exception of CM. High temperature (35 °C) may significantly hasten the release of K⁺ from organic substrates (except for WC) with low temperatures significantly inhibiting release of K⁺ in Sd and CRH. High temperatures (35 °C) might significantly facilitate the release of Na⁺ in CM and TC. However, no significant differences were manifested in the release of Na⁺ from organic substrates at different temperatures, with the exception of CM and TC. Moreover, no significant differences were observed in the release of calcium, magnesium and iron ions with time, nor were there any significant differences in the contents of iron ions in the aqueous extracts of organic materials at different temperatures. The results indicate that multiple mediums should be pretreated in water for a week before being used for planting. They should be used when all mineral elements of organic materials are steady and ignoring the effect of organic mediums.     

Selection of adsorbents for treatment of leachate: batch studies of simultaneous adsorption of heavy metals

The simultaneous adsorption of copper (Cu), cadmium (Cd), nickel (Ni), and lead (Pb) ions from spiked deionized water and spiked leachate onto natural materials (peat A and B), by-product or waste materials (carbon-containing ash, paper pellets, pine bark, and semi-coke), and synthetic materials (based on urea-formaldehyde resins, called blue and red adsorbents) or mixtures thereof was investigated. The adsorbents that gave the highest metal removal efficiencies were peat A, a mixture of peat B and carbon-containing ash, and a mixture of peat A and blue. At an initial concentration of 5 mg/l for each metal, the removal of each species of metal ion from spiked water and spiked leachate solutions was very good (>90%) and good (>75%), respectively. When the initial concentration of each metal in the solutions was twenty times higher (100 mg/l), there was a noticeable decrease in the removal efficiency of Cu²⁺, Cd²⁺, and Ni²⁺, but not of Pb²⁺. Langmuir monolayer adsorption capacities, q_m, on peat A were found to be 0.57, 0.37, and 0.36 mmol/g for Pb²⁺, Cd²⁺, and Ni²⁺, respectively. The order of metal adsorption capacity on peat A was the same in the case of competitive multimetal adsorption conditions as it was for single-element adsorption, namely Pb²⁺ > Cd²⁺ ≥ Ni²⁺. The results show that peat alone (an inexpensive adsorbent) is a good adsorbent for heavy metal ions.     

袋式除尘器气流分布数值计算研究

采用结构化/非结构化混合网格技术、多孔介质模型及k-ε两方程湍流模型,对某袋式除尘器及进出口管道内的气体流场进行了数值计算.计算结果表明,合理布置导流板后,袋式除尘器两箱体流量偏差为1.8％;除尘器下游滤袋单元处理气量偏大,中游滤袋单元处理气量较小,最大流量与最小流量偏差为22.3％;靠近除尘器进口处灰斗内存在气流回流特性,易造成粉尘的二次附着现象.     

Effect of Degree of Substitution of Octenyl Succinate Starch on Enzymatic Degradation

Octenyl succinate starch of degree of substitution (ds) 0.03, 0.07, and 0.11 was synthesized in an aqueous medium. These compounds were then tested for the susceptibility to enzymatic degradation. The multiple-enzyme regime of -amylase, amyloglucosidase, and pullulanase was chosen for the evaluation. This combination of enzymes had been proven to degrade 99.5% of unmodified starch to glucose and hence was chosen for this study. It was found that even small amounts of subsituent caused a considerable decrease in the extent of degradation. The net extent of degradation decreased with increasing ds. Surprisingly, the amount of glucose from all three substituted substrates was quite similar, suggesting the effect small amounts of subtituent had on the enzymatic activity.     

Effect of depth of landfill on the characteristics of soil-like material of aged waste: a case study of Bhalswa dumpsite,India

Journal of Material Cycles and Waste Management - This study characterizes the municipal solid waste (MSW) accumulated for more than 25&nbsp;years at Bhalswa dumpsite, Delhi, India. 50...