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蒸氨氨分解改为磷铵法生产氨水的实践
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作者 黄发亮 《安徽化工》 CAS 2018年第3期92-93,97,共3页
随着焦化行业日益严格的环保要求,尾气治理势在必行,特别是焦化一直沿用的蒸氨氨分解工艺,其氨分解尾气达标排放一直困扰许多企业。结合拜城县众泰煤焦化有限公司煤气净化蒸氨氨汽燃烧分解处理工艺现状,提出实施工艺技术升级和环保改造。
关键词 蒸氨氨汽 磷酸吸收 生产氨水 技改
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磷铵洗氨生产浓氨水工艺研究
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作者 赵博 《燃料与化工》 2023年第3期39-43,共5页
对磷铵洗氨生产浓氨水工艺进行了详细的阐述。对磷铵洗氨生产浓氨水工艺的工艺流程、主要设备、操作参数、操作要点等进行了研究分析,并就生产中常见的问题给出了解决方案。
关键词 磷铵洗氨 氨水生产工艺 磷铵溶液
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完善浓氨水生产工艺流程的几项措施
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作者 亓学山 《山东冶金》 CAS 1997年第S1期50-52,共3页
莱钢焦化厂为解决浓氨水生产工艺流程中的设备腐蚀、泄漏、维修量大、开工率低等问题,采取了以螺旋板换热器代替原列管换热器,以铸铅材质替代铸铁材质,以不锈钢板代替普通钢板,增加吸收塔填料密度等措施,使浓氨水生产工艺开工率达9... 莱钢焦化厂为解决浓氨水生产工艺流程中的设备腐蚀、泄漏、维修量大、开工率低等问题,采取了以螺旋板换热器代替原列管换热器,以铸铅材质替代铸铁材质,以不锈钢板代替普通钢板,增加吸收塔填料密度等措施,使浓氨水生产工艺开工率达99.5%,泄漏率降至0.1%以下。 展开更多
关键词 氨水 氨水生产工艺 效果
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TRACE MODE自适应控制算法在氨水生产流程中的应用
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作者 黎明 《计算机测量与控制》 CSCD 2004年第10期961-964,共4页
通过TRACEMODE工控软件的自适应控制算法和冗余功能在氨水生产流程中的应用,介绍了以工业控制计算机为硬件平台的冗余控制系统方案以及TRACEMODE软件中自适应控制算法和冗余功能的实现原理。实际应用表明,基于TRACEMODE的控制系统具有... 通过TRACEMODE工控软件的自适应控制算法和冗余功能在氨水生产流程中的应用,介绍了以工业控制计算机为硬件平台的冗余控制系统方案以及TRACEMODE软件中自适应控制算法和冗余功能的实现原理。实际应用表明,基于TRACEMODE的控制系统具有可靠性高、自适应PID控制品质优异的特点。 展开更多
关键词 自适应控制算法 氨水生产流程 TRACE MODE 控制系统 工业控制计算机 PID
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尿素装置氨水与解吸废液综合利用措施及其效益 被引量:1
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作者 王付生 李秀琴 《中氮肥》 2015年第3期43-44,68,共3页
介绍尿素装置氨水与解吸废液的产生及常规处理情况,结合六国化工的生产实际,探讨将氨水与解吸废液用于锅炉烟气脱硫、气化磨煤、循环水池、氨水生产系统等综合利用措施及其效益。
关键词 尿素装置 氨水 解吸废液 锅炉烟气脱硫 气化磨煤 循环水池 氨水生产系统 综合利用效益
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Extraction of Theanine from Waste Liquid of Tea Polyphenol Production in Aqueous Two-phase Systems with Cationic and Anionic Surfactants 被引量:8
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作者 张军伟 王艳 彭奇均 《Chinese Journal of Chemical Engineering》 SCIE EI CAS CSCD 2013年第1期31-36,共6页
Extraction of theanine from waste liquid of tea polyphenol production was studied in aqueous surfactanttwo-phase system (ASTP) with cationic surfactant (CTAB) and anionic surfactant (SDS). Results indicate that ... Extraction of theanine from waste liquid of tea polyphenol production was studied in aqueous surfactanttwo-phase system (ASTP) with cationic surfactant (CTAB) and anionic surfactant (SDS). Results indicate that the region of ASTP is narrow and there is only a two-phase region of cationic surfactant. The increase in concentrations of NaBr and Na2SO4 are beneficial to the formation of ASTP. Theanine concentration in the bottom phase increases with increasing concentration of theanine, whereas the Partition coefficient and extraction rate only change a littlewhen the concentration of theanine is above 0.2 g.L-'. With the increase of SDS concentration, the phase ratio and the partition coefficient decrease, while the extraction efficiency of theanine increases and the concentration of theanine changes a little in the range from 2.4/7.5 to 2.8/7.2 for SDS/CTAB ratio. The temperature has a notable ef- fect on the concentration of theanine in the bottom phase, partition coefficient and extraction rate of theanine. The increase of waste liquid decreases the phase ratio, increases the concentration and extraction rate of theanine in the bottom ohase, since the orotein and the saccharide enter the bottom nhase with theanine. 展开更多
关键词 aqueous two-phase system SURFACTANT THEANINE waste liquid of tea polyphenol production EXTRACTION
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On the Production of OH Radical through Plasma Electrolysis Mechanism for the Processing of Ammonia Waste Water
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作者 Setijo Bismo Knsna Irawan Eva Fathul Karamah Nelson Saksono 《Journal of Chemistry and Chemical Engineering》 2013年第1期6-12,共7页
Plasma produced many active species such as OH radical and H radical. As well known, OH radical plays an important role in degrading complex pollutants. This study aims to measure the production of OH radicals and eva... Plasma produced many active species such as OH radical and H radical. As well known, OH radical plays an important role in degrading complex pollutants. This study aims to measure the production of OH radicals and evaluate important parameters that have influent in degradation process of waste water contains ammonia in circulated system and analyze the level of energy consumptions are resulted by this research. The production of OH radical was detected by formation of hydrogen peroxide which was resulted by recombination reaction between OH radicals during plasma electrolysis process. From the measured concentration of hydrogen peroxide, obtained concentration of OH radical is 2,020 ppm. The depth of anode, applied voltage and ammonia initial concentration have affected ammonia degradation percentage and energy consumption level. The highest result for ammonia degradation percentage is 63.2% which gets from applied voltage 700 V, with depth of anode 1 cm, initial concentration of ammonia 100 ppm, and lowest energy consumption of 110 KJ/mmol. 展开更多
关键词 Plasma electrolysis OH radical ammonia.
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