乙烯废碱液综合治理技术探讨

分析了乙烯裂解气碱洗过程所排放废液的组成及性质，讨论了该废液的除油方法及综合治理和利用的途径。     

废干电池浸出的试验研究

以锌碳电池和碱性锌锰电池为实验对象，通过固体废物浸出毒性试验，探讨废电池在不同破坏程度、不同pH值和不同浸取级数条件下的浸出规律。试验发现，锌碳电池中Pb、Cd、zn、Mn浸出浓度相对较高，碱性锌锰电池中Cu、As、Hg浸出浓度较高。对于锌碳电池，中性浸取剂和酸性浸聚剂影响不大，而对于碱性锌锰电池，酸性浸取剂条件下浸浓度反而较低。锌碳电池和碱性锌锰电池都是在完全破坏条件下浸出浓度高。在实际中，电池外壳腐蚀是一个缓慢的过程。     

Chemical and process mineralogical characterizations of spent lithium-ion batteries: An approach by multi-analytical techniques

Mineral processing operation is a critical step in any recycling process to realize liberation, separation and concentration of the target parts. Developing effective recycling methods to recover all the valuable parts from spent lithium-ion batteries is in great necessity. The aim of this study is to carefully undertake chemical and process mineralogical characterizations of spent lithium-ion batteries by coupling several analytical techniques to provide basic information for the researches on effective mechanical crushing and separation methods in recycling process. The results show that the grade of Co, Cu and Al is fairly high in spent lithium ion batteries and up to 17.62 wt.%, 7.17 wt.% and 21.60 wt.%. Spent lithium-ion batteries have good selective crushing property, the crushed products could be divided into three parts, they are Al-enriched fraction (+2 mm), Cu and Al-enriched fraction (?2 + 0.25 mm) and Co and graphite-enriched fraction (?0.25 mm). The mineral phase and chemical state analysis reveal the electrode materials recovered from ?0.25 mm size fraction keep the original crystal forms and chemical states in lithium-ion batteries, but the surface of the powders has been coated by a certain kind of hydrocarbon. Based on these results a flowsheet to recycle spent LiBs is proposed.     

A preliminary process design and economic assessment of a catalyst rejuvenation process for waste disposal of refinery spent catalysts

Spent hydroprocessing catalysts from refineries have been classified as hazardous solid waste by the United States Environmental Protection Agency (USEPA), refiners must find a viable but economical solution to solve this serious environmental issue. Catalyst rejuvenation is an attractive option for minimizing the environmental problems associated with spent catalysts. In this study, a preliminary design for such a process and the corresponding economic analysis are performed to assess the proposed catalyst rejuvenation process for metal-fouled spent catalysts generated in residue hydroprocessing units. The scenarios used in the economic assessment are based on three options of process synthesis and two operator modes. It is found that the option of rejuvenating medium and lightly fouled spent catalyst produced by the refinery will be the best solution for refiners, both environmentally and economically.     

洗浴用小型锅炉的测试与评价

经过多次对煤炭气化高温蒸汽锅炉、型煤锅炉、常压反烧锅炉和蒸汽锅炉等洗浴用小锅炉的测试、分析与评价,确认煤炭气化高温蒸汽锅炉的节能环保指标都比其他锅炉具有显著的优越性。它可以在常压下产生150℃的高温蒸汽,燃烧散煤时其排放的SO2和烟尘都达到国家一级排放标准,锅炉平均热效率可达78.05%,比同吨位的常压热水锅炉和蒸汽锅炉节能30%,比型煤锅炉节能约50%,比燃油锅炉、燃气锅炉、电锅炉节能约60%以上。     

An unconventional method for the recovery of caustic soda from spent Al-rich pickling solutions

This work presents an unconventional procedure for the recovery of spent Al-rich caustic soda solutions from the pickling of dies for the production of aluminium extrusions. Caustic soda was regenerated at roughly 70%, by precipitating aluminate, after addition of a silica source, in the form of zeolite A, a microporous material that is widely used in many technological sectors. It was shown that the process is reliable and can be repeated for several cycles, provided the concentration of the caustic soda solution is suitably restored. The by-product obtained, zeolite A, proved to be a high-grade material with performance as a cation exchanger and physical sorbent that is certainly comparable to that reported in literature (e.g., cation exchange capacity equal to 5.14 meq g(-1) vs. 5.48 meq g(-1) and water vapour adsorption capacity of 26.5% vs. 27.6% at 16 torr and 298 K). The economics of the process, although not examined yet, would appear generally favourable, considering that zeolite A is a valuable by-product which widely covers the costs for the recovery of the spent solutions. There are, therefore, significant prospects for the use of zeolite A, particularly as a builder in detergent formulation.     

A mechanical pre-treatment process for the valorization of useful fractions from spent batteries

In this paper the authors propose a full-scale plant aimed to pre-treat spent batteries in order to obtain cleaned useful fractions (magnetic and non-magnetic metals, paper, plastic, a fine-sized material made of a metal-carbon mixture). The treating process was designed after having analyzed and tested a representative sample coming from the whole amount of spent batteries collected in 1 month by the public service in and around Turin. The analyses performed on the sample allowed the authors to determine its in-percentage composition in term of type of batteries: 60-70% b.w. (by weight) alkaline, 25-30% b.w. Zn-C and 5-10% b.w. other types. For each type, the composition in term of size (AAA or LR03; AA or LR6; C or LR14; D or LR20; 9 V or 6F22A; 4.5 V or 3R12A) has also been determined.The treatment for the recovery of secondary raw materials foresees the following phases:

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separation of useful types/sizes of exhaust batteries to undergo further treatments by means of a first sieving process;

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liberation of the single components taking advantage of a crushing operation;

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separation of a fine-sized material (to subject to pyro or hydro metallurgic recovery) from a coarse-sized material (to send to secondary smelt foundries and incinerators) by means of a second sieving phase.

On the basis of the results obtained from the crushing/sieving laboratory tests and the chemical characterization, a full-scale plant able to treat about 76,000 t/y of spent batteries has been designed. The cost analysis performed on the proposed treatment plant has given back a unit pre-treatment cost equal to 3€ per ton of processed spent batteries.     

High performance of multi-layered alternating Ni–Fe–P and Co–P films for hydrogen evolution

Judiciously engineering the electrocatalysts is attractive and challenging to exploit materials with high electrocatalytic performance for hydrogen evolution reaction. Herein, we successfully perform the interface engineering by alternately depositing Co–P and Ni–Fe–P films on nickel foam, via facile electroless plating and de-alloying process. This work shows that there is a significant effect of de-alloying process on alloy growth. The electronic structure of layered alloys is improved by interface engineering. The multilayer strategy significantly promotes the charge transfer. Importantly, the Co–P/Ni–Fe–P/NF electrode fabricated by interface engineering exhibits excellent electrocatalytic hydrogen evolution activity with an overpotential of 43.4 mV at 10 mA cm-2 and long-term durability for 72 h in alkaline medium (1 mol L-1 KOH). The innovative strategy of this work may aid further development of commercial electrocatalysts.     

乙烯裂解废碱氧化影响因素分析

就影响独山子石化公司乙烯裂解装置废碱液氧化反应的因素，在实验室小试规模试验的基础上，对影响因素进行分析和探讨，着重分析了装置在运行过程中出现的问题和存在的不足，在对现有装置工艺不做大的改动的前提下，提出了装置的技术改造建议。     

硼氢化钠还原法处理化学镀镍废液

采用硼氢化钠作为还原剂处理化学镀镍废液。研究了硼氢化钠投加量、反应时间、温度及pH对镍处理效果的影响。试验表明，投加一定量硼氢化钠溶液，控制pH为6、温度为50℃，反应10min后可以将废液中的镍由6000mg/L降至10mg/L以下。每升废液可获得54g淀淀物，其中镍质量分数达到66.1%。