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硫酸生产排出的尾气含有0.3—0.5%的二氧化硫和少量的三氧化硫。如果不回收利用,不仅浪费资源,而且污染大气。株州化工厂将硫酸尾气进行了回收,制成液体二氧化硫。液体二氧化硫是生产锦纶和医药的重要原料,副产品硫铵母液是很好的肥料,同时还可生产亚硫酸铵代替烧碱作为造纸工业的原料,做到了化害为利,变废为宝。 液体二氧化硫的生产工艺,是采用氨水吸收硫酸尾气中二氧化硫、三氧化硫生成循环母液,然后用93%硫酸分解循环母液,产 相似文献
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刘坤业 《石油化工环境保护》1985,(1)
我厂生产凡士林、白油采用老工艺(三氯化铝精制和酸精制)。间断生产过程排放出尾气中含有SO_2、SO_3、Hcl等酸性气体,其浓度瞬间超过国家标准,操作工人需戴防毒面具在恶劣环境中工作.必须采取措施积极予以治理. 一九八○年采用加高烟囱排放,由于SO_2未经净化,飘落扩散至厂区及居民区造成污染及危害.最后决定采用波纹填料喷淋塔,用 相似文献
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一、前言天津海豚炭黑有限公司现有两台额定蒸发量为15t/h的发电锅炉,即3#发电锅炉和4#发电锅炉,所使用的燃料为炭黑生产炉产生的尾气。3#发电锅炉是以5#生产炉的尾气作为燃料,4#发电锅炉是以6#生产炉的尾气作为燃料(见图1)。随着5#、6#炭黑生产炉设备的日益老化,当其中一条生产线因 相似文献
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祁春生 《安全.健康和环境》1995,(4)
尿素尾气系统的防爆措施山西焦化工业总公司祁春生水溶液全循环法生产尿素的中氮肥企业,在二氧化碳原料气脱氢装置未能推广的情况下,在正常生产过程中,惰性气体器出口气和尾气吸收塔出口气中,氨、氧、氢、甲烷等主要组分能够形成爆炸性混合气体,这是水溶液全循环生产... 相似文献
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6月5日一座具有国内先进水平的沥青尾气焚烧炉在齐鲁石化公司胜利炼油厂点火投用.胜利炼油厂是我国最大的沥青生产基地,每年生产各种沥青近70万吨.原有旧沥青尾气焚烧炉工艺落后、焚烧率低.为了根治沥青尾气污染、保护环境,1994年胜利炼 相似文献
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普钙生产过程中,当磷矿粉和硫酸在混合反应时,伴有大量废水逸出,如四氟化硅、氟化氢、二氧化碳、二氧化硅等,其中氟化氢、四氰化硅都具有强烈刺激性臭味,对人体十分有害(刺激眼、鼻、破坏皮肤、骨骼)。生产一吨普钙排出的废气达300m~3左右,含氟量为20g/m~3废气。普钙工厂排出的含氟气体通常回 相似文献
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上海染料化工厂采取各种切实有效的技术措施,治理硝酸尾气,减少了闵行地区的大气污染。该厂将在硝酸生产、氧化吸收过程中产生的 NO 气体,经两座氧化吸收填料塔,用碱液送流、吸收 NO_x 后 相似文献
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在硫酸系统中,通过水平衡分析计算烟气带入净化工序的SO2体积分数和含水量,确定净化工序的能力,控制干燥塔进口烟气温度,使干吸工序生产出合格产品;通过计算,烟气带入净化工序的水量小于产品带出的水量,制酸净化污水经过污水处理工序处理后返回到净化工序重复使用,实现净化污水零排放,消除对环境的污染. 相似文献
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《Atmospheric Environment. Part A. General Topics》1990,24(10):2699-2702
As part of the Southern California Air Quality Study (SCAQS), ambient levels of gas phase formic acid and acetic acid have been measured at four locations: a ‘control’ site (San Nicholas Island), a source-dominated coastal site (Long Beach) and two inland smog receptor sites (Claremont and Palm Springs). Samples were collected on alkaline traps and were analyzed by size exclusion liquid chromatography with ultraviolet detection. Levels of gas phase formic acid (up to 19 ppb) and acetic acid (up to 17 ppb) exhibited diurnal (frequent night-time maxima), spatial and seasonal variations. During summer smog episodes, concentrations increased from 0.6 ppb at the ‘control’ site to up to 13–19 ppb at the inland smog receptor sites reflecting primary emissions and in situ formation during transport inland. The acetic acid/formic acid (A/F) ratio decreased from coastal to inland sites. At the coastal site levels of both acids and the A/F ratio were substantially higher during the fall than during the summer. 相似文献
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Formic acid was used for the nitrate reduction as a reductant in the presence of Pd:Cu/γ-alumina catalysts. The surface characteristics of the bimetallic catalyst synthesized by wet impregnation were investigated by SEM, TEM-EDS. The metals were not distributed homogeneously on the surface of catalyst, although the total contents of both metals in particles agreed well with the theoretical values. Formic acid decomposition on the catalyst surface, its influence on solution pH and nitrate removal efficacy was investigated. The best removal of nitrate (50 ppm) was obtained under the condition of 0.75 g/L catalyst with Pd:Cu ratio (4:1) and two fold excess of formic acid. Formic acid decay patterns resembled those of nitrate removal, showing a linear relationship between kf (formic acid decay) and k (nitrate removal). Negligible amount of ammonia was detected, and no nitrite was detected, possibly due to buffering effect of bicarbonate that is in situ produced by the decomposition of formic acid, and due to the sustained release of H2 gas. 相似文献
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金属掺杂二氧化钛光催化还原硝酸氮 总被引:5,自引:0,他引:5
采用光沉积法制备了负载金属Fe或Cu的P25二氧化钛光催化剂,用TEM、ICP、XRD及UV-Vis等对其进行了表征,并测定其在20 W紫外灯照射下光催化还原硝酸氮、去除总氮的效果;考察了pH值、搅拌气体、金属的负载量、空穴清除剂甲酸的用量以及金属Ag-Cu复合沉积等条件的影响.反应2 h的结果表明,二氧化钛上载铜量增加,硝酸氮转化率随之增加,但最大总氮去除率和氮气选择性均出现在0.5%Cu负载量下;氮气搅拌和酸性条件下反应,形成氮气的选择性略低(62%),但最高的硝酸氮转化率和总氮去除率分别达到36.9%和23.2%;CO2作为搅拌气体.Cu的负载量为0.5%、甲酸用量为0.06 mol/L时.形成氮气选择性最好(88.4%).硝酸氮转化率和总氮去除率分别为29.5%和25.1%.同样条件下,采用二氧化钛上共沉积金属总质量分数为1%、Ag:Cu=1:1的催化剂,硝酸氮的转化率可达48.1%,总氮去除率为34.2%,氮气选择性为72.2%. 相似文献
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The low-heat-value cornstalk gas produced in the down-flow fixed bed gasifier was tentatively used for methanol synthesis. The cornstalk gas was purified and the technical procedures such as deoxygenation, desulfurization, catalytic cracking of tar, purification and hydrogenation were studied. The catalytic experiments of methanol synthesis with cornstalk syngas were carried out in a tubular-flow integral and isothermal reactor. The effect of reaction temperature, pressure, catalysttypes, catalyst particle size, syngas flow at entering end and composition of syngas was investigated. The optimum process conditions and yield of methanol from cornstalk syngas were obtained. The experimental results indicated that the proper catalyst of the synthetic reaction was C301 and the optimum catalyst size (φ) was 0.833 mm×0.351 mm. The optimum operating temperature and pressure were found to be 235℃ and 5 Mpa, respectively. The suitable syngas flow 0.9-1.10 mol/h at entering end was selected and the best composition of syngas were CO 10.49%, CO2 8.8%, N2 37.32%, CnHm 0.95% and H2 40.49%. The best methanol yield is 0.418 g/g cornstalk. The study provided the technical support for the industrial test of methanol production from biomass (cornstalk)gas. 相似文献
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碱性树脂吸附碳酸氢盐水溶液中甲酸的研究 总被引:1,自引:0,他引:1
采用静态法测定了5种树脂对碳酸氢钾溶液中甲酸的交换吸附量,其中,D293强碱性阴离子交换树脂具有最高的交换吸附量,考察了温度对D293树脂交换吸附量的影响。在30℃条件下,利用静态法测定了甲酸在D293树脂上的吸附等温线,在低的甲酸浓度范围内,Langmuir方程比Freundlich方程能更好地描述树脂对甲酸的吸附;同时,测定了甲酸在D293树脂上的穿透曲线。 相似文献