用亚氨基二乙酸盐酸盐废液作冷冻剂

1.概述亚氨基二乙酸盐酸盐(简称二酸盐)是合成除草剂草甘膦的一个中间体。每生产1吨100%的二酸盐就有10吨废母液产生,排弃后造成环境污染。关于二酸盐废母液的利用,国内尚未见有报道。1985年8月我厂进行了利用二酸盐废母液作冷冻剂的研究,并于同年10月利用研究成果建成了一套处理装置。用处理后的二酸盐废母液作冷冻剂,用于实际生产,取得了十分满意的经济效果。     

日本废塑料作为原料再生利用的技术简介

1 废塑料不如废金属作为原料再生利用好的原因 金属报废后作为原料再生利用已广泛在汽车、饮料容器等方面作到广泛应用,而和金属同样做为原材料的塑料报废后作原料再生利用的却很少.如在日本1995年废塑料的再生利用率达 36%时,作为原料再生的仅12%,而且大部是塑料加工过程中产生的废物,包装容器等报废的极少;而同期废金属罐壳作金属原料再生利用的却达70%左右,差距太大.初步分析有以下原因:     

絮凝-树脂吸附法处理高色度邻硝基苯胺废水

采用絮凝－树脂吸附法处理高色度邻硝基苯胺废水,比较了不同絮凝剂的处理效果。试验结果表明,用硫酸铝作絮凝剂,以生石灰作助凝剂,加入少量高分子絮凝剂进行絮凝沉降处理,然后用ＣＨＡ－１０１树脂进行吸附处理,处理后废水色度由≥１６０００倍降至４０倍以下,ＣＯＤ由≥５０００ｍｇ／Ｌ降至≤８０ｍｇ／Ｌ,ＰＨ６～７。     

间苯氧基甲苯生产废水和废渣的综合利用

对间苯氨基甲苯生产废水和废渣的处理及回收工艺作了介绍。废渣中各组分经分离后全部回收利用；废水经二级萃取脱酚处理后用于普钙生产，回收了有用物质，可取得明显的经济效益和环境效益。     

管桩余浆的合理开发利用

对管桩余浆常用的几种回收利用方法作了分析对比,提出了较为完善的余浆干法利用方法,将余浆固化后经破碎、烘干、粉磨,再用作混凝土的掺合料,更加有利于发挥余浆的潜在活性.     

用柴油吸收法治理熬炼废气

本文介绍用柴油作吸收剂处理熬炼废气的原理、工艺流程和影响处理效果的因素。其处理工艺简单、处理效果稳定可靠,能比较彻底地解决熬炼废气的污染问题。吸收废气后的柴油仍可供燃料使用。     

膨润土的改性及在废水处理中的应用

膨润土具有良好的体积膨胀性、离子交换性和吸附性,在环境保护特别是废水处理中有较大的应用前景,目前主要经改性后应用于重金属离子和有机污染物的去除.对膨润土改性及其在废水处理中的应用现状作了综述.     

混床在电厂除盐水处理中的设计探讨

结合天津第一热电厂给水处理技改工程,对利用河水处理后用于锅炉补给水除盐工艺中混床的原理和操作运行作了具体分析,对混床设计中需注意的事项进行了探讨,为电厂除盐水处理设计运行提供参考.     

废铁屑—H2O2法处理炼油厂含酚废水

用废铁屑作催化剂，Ｈ２Ｏ２作氧化剂，对炼厂汽提后含硫废水进行了除酚试验研究，考察了初始ＰＨ、Ｈ２Ｏ２投加量、废铁屑投加量对酚去除率的影响。对含酚量为３３１．５ｍｇ／Ｌ的废水，将其初始ＰＨ调至７．２，３０％Ｈ２Ｏ２的投加量为７．５ｍＬ／Ｌ，废铁屑的投加量为３－８ｇ／Ｌ，经２ｈ反应后，酚的脱除率可达９９．９％。     

脉冲除尘器在钙镁磷肥粉磨除尘中的应用

1 前言钙镁磷肥的生产是以磷矿为原料,白云石为熔剂,焦炭作燃料,在高炉中经高温熔融后,熔料经水淬骤冷成为1-3mm的粒状半成品,再经自然沥水后烘干,用球磨机磨成一定粒度的粉末,包装后即为成品。在磨制和包装过程中,球磨机尾部排气筒及包装口的粉尘排放到空气中,岗位粉尘浓度曾高达100mg/m~3,不仅严重危害了职工的身体健康,而且也浪费了磷肥资源。我     

Waste catalysts for waste polymer

Catalytic cracking of high-density polyethylene (HDPE) over fluid catalytic cracking (FCC) catalysts (1:6 ratio) was carried out using a laboratory fluidized bed reactor operating at 450 degrees C. Two fresh and two steam deactivated commercial FCC catalysts with different levels of rare earth oxide (REO) were compared as well as two used FCC catalysts (E-Cats) with different levels of metal poisoning. Also, inert microspheres (MS3) were used as a fluidizing agent to compare with thermal cracking process at BP pilot plant at Grangemouth, Scotland, which used sand as its fluidizing agent. The results of HDPE degradation in terms of yield of volatile hydrocarbon product are fresh FCC catalysts>steamed FCC catalysts approximately used FCC catalysts. The thermal cracking process using MS3 showed that at 450 degrees C, the product distribution gave 46 wt% wax, 14% hydrocarbon gases, 8% gasoline, 0.1% coke and 32% nonvolatile product. In general, the product yields from HDPE cracking showed that the level of metal contamination (nickel and vanadium) did not affect the product stream generated from polymer cracking. This study gives promising results as an alternative technique for the cracking and recycling of polymer waste.     

Synthesis of chromium-containing pigments from chromium recovered from leather waste

Cobalt-chromite green and chrome-tin pink pigments have been prepared from chromium extracted from leather shavings produced as a waste product of the leather-tanning industry. The alkaline agent (NaOH, CaO, MgO, NH4OH) used in the extraction process influences the nature of the final product. The effect of the NH4OH:CaO ratio on the final product in the case of cobalt-chromite green was examined. The pigments obtained were characterized by FT-IR and X-ray diffraction (XRD). Colour measurements were compared with those recorded from materials prepared from pure Cr2O3. The leaching of Cr(VI) from the materials was examined by UV spectroscopy.     

Landfill gas upgrading with countercurrent water wash

A pilot-scale countercurrent absorption process for upgrading landfill gas to produce vehicle fuel was studied using absorption and desorption units and water as absorbent. The height-to-diameter ratio of the absorption column used was 3:1 instead of the more conventionally used 20:1 ratio, and a higher pressure was used along with a lower water flow rate. The effects of pressure (10-30bar) and water and gas flow-ratios on the upgrading process were studied. Methane content in the product gas increased to near or above 90% with both gas flows (50 and 100l/min) used at over 20bar pressure with 10l/min water flow and at 30bar pressure with 5l/min water flow. Carbon dioxide content with these upgrading parameters ranged from 3.2% to 4.8%. The remaining fraction of the product gas was nitrogen (from 6% to 7%), while hydrogen sulphide was removed to below the detection limit with all of the upgrading parameters used. The methane content of exhaust gas increased with increasing pressure. In conclusion, the pilot-scale gas upgrading process studied here appears to be able to produce gas with high energy content (>90% methane), apparently suitable as vehicle fuel, from landfill gas.     

Transesterification reaction of the fat originated from solid waste of the leather industry

The leather industry is an industry which generates a large amount of solid and liquid wastes. Most of the solid wastes originate from the pre-tanning processes while half of it comes from the fleshing step. Raw fleshing wastes which mainly consist of protein and fat have almost no recovery option and the disposal is costly. This study outlines the possibility of using the fleshing waste as an oil source for transesterification reaction. The effect of oil/alcohol molar ratio, the amount of catalyst and temperature on ester production was individually investigated and optimum reaction conditions were determined. The fuel properties of the ester product were also studied according to the EN 14214 standard. Cold filter plugging point and oxidation stability have to be improved in order to use the ester product as an alternative fuel candidate. Besides, this product can be used as a feedstock in lubricant production or cosmetic industry.     

Prediction of unconfined compressive strength of cement paste containing industrial wastes

Neural network analysis was used to construct models of unconfined compressive strength (UCS) as a function of mix composition using existing data from literature studies of Portland cement containing real industrial wastes. The models were able to represent the known non-linear dependency of UCS on curing time and water content, and generalised from the literature data to find relationships between UCS and quantities of five waste types. Substantial decreases in UCS were caused by all wastes; except for EAF dust, the effect was nonlinear with the greatest decrease caused initially by approx. 12% plating sludge, 40% foundry dust, 58% other ash, and 72% MSWI fly ash by mass of dry product. It appears that the maximum waste additions used in modelling may approximate the practical limits of waste additions used in modelling may approximate the practical limits of waste addition to Portland cement, i.e., 50% plating sludge or EAF dust, 64% foundry dust, 92% other ash, and 85% MSWI fly ash by mass of dry product. The laboratory was found to be a key predictive variable and acted as a surrogate for laboratory-specific variables related to cement composition, strength and hardening class, product mixing and preparation details, laboratory conditions, and testing details. While the neural network modelling approach has been shown to be feasible, development of better models would require larger data sets with more complete information regarding laboratory-specific variables and waste composition.     

改性蚁酸木质素的制备与应用

采用加拿大一枝黄花茎杆为原料提取蚁酸木质素，通过氧化或接枝复合的方法对蚁酸木质素进行改性，对改性产物进行了FTIR和SEM表征。实验结果表明：接枝复合改性产物中存在-CONH的接枝复合链，氧化改性产物基本保持了蚁酸木质素原来的吸收峰；采用接枝复合改性产物处理初始质量浓度为50 mg/L的亚甲基蓝废水，在废水pH 7、吸附时间4 h、改性产物加入量22 mg/mL的条件下，亚甲基蓝去除率为90.94%；采用氧化改性产物处理相同亚甲基蓝废水，在废水pH 10、吸附时间12 h、改性产物加入量22 mg/mL的条件下，亚甲基蓝去除率为81.93%。     

Environmental and Cost Assessment of a Polypropylene Nanocomposite

This paper describes a study on the use of a polypropylene (PP)/layered silicate nanocomposite as packaging film, agricultural film, and automotive panels. The study’s main question was “Are the environmental impacts and costs throughout the life cycle of nanocomposite products lower than those of products manufactured from conventional materials?” The conventional (benchmark) materials studied were pure polypropylene as packaging film, pure polyethylene as agricultural film, and glass fiber-reinforced polypropylene as automotive panels. In all three cases, the use of the PP nanocomposite resulted in a reduction of the amount of material used, while ensuring the same functionality. Material reduction was estimated using Ashby’s material indices and amounted to ?9% for packaging film, ?36.5% for agricultural film, and ?1.25% for automotive panels. It goes without saying that a product’s impact on the environment will decrease when less material is used. The production and incorporation of nanoparticles, however, may have additional impacts. We found clear environmental benefits throughout the entire life cycle when the PP nanocomposite is used in the manufacture of agricultural film. We noted some cost benefits when the nanocomposite is used in the production of agricultural film and automotive panels. If the price of nanoclay is at most €5,000 tonne then the cost of nanocomposite packaging film is also lower than that of the conventionally produced product.     

Composting of waste algae: A review

Although composting has been successfully used at pilot scale to manage waste algae removed from eutrophied water environments and the compost product applied as a fertiliser, clear guidelines are not available for full scale algae composting. The review reports on the application of composting to stabilize waste algae, which to date has mainly been macro-algae, and identifies the peculiarities of algae as a composting feedstock, these being: relatively low carbon to nitrogen (C/N) ratio, which can result in nitrogen loss as NH₃ and even N₂O; high moisture content and low porosity, which together make aeration challenging; potentially high salinity, which can have adverse consequence for composting; and potentially have high metals and toxin content, which can affect application of the product as a fertiliser. To overcome the challenges that these peculiarities impose co-compost materials can be employed.     

Evaluation of a chemical stabilization process

Environmental Resources Management (ERM) performed an evaluation of a biosolids chemical stabilization process known as BIO*FIX®, marketed by Bio Gro Systems, Inc., of Annapolis, Maryland. The purpose of the evaluation was (1) to assess major characteristics of the process and its final product, (2) to determine the quantity and final disposition of all components in the incoming biosolids, and (3) to determine if the process conforms to new regulations promulgated and administered by the U.S. Environmental Protection Agency (EPA) titled “Standards for the Use or Disposal of Sewage Sludges” (40 CFR Part 503). The BIO*FIX® chemical stabilization process involves the addition of calcium oxide (CaO) to dewatered biosolids at rates that achieve the pathogen reduction and vector attraction reduction requirements of the 503 program while creating a marketable end product used as an agricultural amendment. ERM's project involved the testing of four process streams in order to create a mass balance on the process. Laboratory analyses were performed on samples of the dewatered biosolids, the chemically-stabilized end product, and the scrubber water effluent. The primary components of concern tested in the above process streams were ammonia, metals, odorous compounds, particulate matter, and organic matter. Through the tests described in the article, ERM drew the following conclusions: (1) The major gaseous pollutant resulting from the BIO*FIX® process is gaseous ammonia. The total gaseous ammonia released from the product depends on the ammonia nitrogen content of the biosolids, and pH and temperature levels reached in the process. Additional ammonia is emitted when the end product is loaded in trucks and stored. Any gaseous ammonia remaining in the end product after processing will slowly dissipate over time. (2) Other potential odor pollutants such as hydrogen sulfide (H₂S) and mercaptans were found to be below detectable levels in the uncontrolled exhaust gas. (3) Metals were not found in the exhaust gas in any detectable quantities. They would not be expected to volatilize during the process. Particulate matter emissions were found to be very low. (4) The pathogen reduction and vector attraction reduction requirements of the 40 CFR 503 regulations were met or exceeded. (5) Finally, through observations and tests, ERM found that the BIO*FIX® chemical stabilization process provides for a simple, viable, and effective conversion of biosolids into a beneficial use product in compliance with all pertinent regulations.     

Measuring the gypsum content of C&D debris fines

Construction and demolition (C&D) debris recycling facilities often produce a screened material intended for use as alternative daily cover (ADC) at active landfills or for shaping and grading at closed landfills. This product contains soil and small pieces of wood, concrete, gypsum drywall, shingles and other components of C&D debris. Concerns have been raised over the contribution of gypsum drywall in C&D debris fines to odor problems at landfills where the product is used. To address such concerns, limitations may be placed on the percentage of gypsum (or sulfate) that can occur, and standardized testing procedures are required to permit valid compliance testing. A test procedure was developed for measuring the gypsum content in C&D debris fines. The concentration of sulfate leached in an aqueous solution was used to estimate the initial gypsum content of the sample. The impact of sample size and leaching time were evaluated. Precision and accuracy increased with increasing gypsum content. Results from replicate samples had an average relative standard deviation of 9%. The gypsum content of fines obtained from different facilities in the US varied widely from 1% to over 25%. These variations not only occurred between differing facilities, but within batches produced within a single facility.