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注射用醋酸亮丙瑞林微球联合左炔诺孕酮宫内缓释系统治疗子宫腺肌症的临床疗效研究
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作者 张亚娟 《中文科技期刊数据库(文摘版)医药卫生》 2024年第2期0135-0138,共4页
浅析在子宫腺肌症临床治疗中采取注射用醋酸亮丙瑞林微球联合左炔诺孕酮宫内缓释系统干预的作用效果。方法 样本对象为60例于2022年2月至2023年2月期间在我科室接受治疗的子宫腺肌症患者,根据治疗方式分为对照组及研究组,对照组28例单... 浅析在子宫腺肌症临床治疗中采取注射用醋酸亮丙瑞林微球联合左炔诺孕酮宫内缓释系统干预的作用效果。方法 样本对象为60例于2022年2月至2023年2月期间在我科室接受治疗的子宫腺肌症患者,根据治疗方式分为对照组及研究组,对照组28例单一接受左炔诺孕酮宫内缓释系统治疗,研究组32例患者在对照组的基础上加入注射用醋酸亮丙瑞林微球治疗。两组治疗3个月后对比疗效、病灶及子宫体积变化以及激素水平。结果 研究组的总有效率为96.87%,明显高于对照组的78.57%;研究组的病灶和子宫体积均小于对照组(P<0.05);研究组雌二醇以及促黄体生成素等激素水平改善优于对照组。结论 在子宫腺肌症的临床治疗中使用注射用醋酸亮丙瑞林微球联合左炔诺孕酮宫内缓释系统干预效果较为理想,可促进患者机体恢复,值得推荐使用。 展开更多
关键词 子宫腺肌症 醋酸亮丙瑞林微球联合左炔诺孕酮宫内缓释系统 临床疗效 子宫体积
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聚乙烯醇车间醋酸系统能量优化
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作者 胡丞 《石油和化工节能》 2010年第3期27-30,19,共5页
通过认真分析聚乙烯醇车间醋酸乙烯和聚乙烯醇两套生产装置独立醋酸精馏系统的特点,优化醋酸精馏系统的运行方式,实现流程再造,将两套生产装置的醋酸精馏系统优化整合,并合理利用醋酸乙烯装置精馏塔采出精醋酸的热能,从而有效降低... 通过认真分析聚乙烯醇车间醋酸乙烯和聚乙烯醇两套生产装置独立醋酸精馏系统的特点,优化醋酸精馏系统的运行方式,实现流程再造,将两套生产装置的醋酸精馏系统优化整合,并合理利用醋酸乙烯装置精馏塔采出精醋酸的热能,从而有效降低装置能耗. 展开更多
关键词 醋酸精馏系统 流程再造 能量优化 降低能耗
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优化整合VAC和PVA装置醋酸精馏系统降低装置能源消耗 被引量:1
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作者 何华祥 《天然气化工—C1化学与化工》 CAS CSCD 北大核心 2011年第4期56-59,共4页
分析了四川维尼纶厂VAC和PVA两套生产装置的设计缺陷,并结合这两套独立运行的醋酸精馏系统的特点,将两套生产装置的醋酸精馏系统进行优化整合,同时优化这两套系统的运行方式,并采取措施充分地利用好VAC装置精馏塔出来的精醋酸的热能,从... 分析了四川维尼纶厂VAC和PVA两套生产装置的设计缺陷,并结合这两套独立运行的醋酸精馏系统的特点,将两套生产装置的醋酸精馏系统进行优化整合,同时优化这两套系统的运行方式,并采取措施充分地利用好VAC装置精馏塔出来的精醋酸的热能,从而达到了有效降低单位产品能耗的目的。 展开更多
关键词 优化整合 醋酸精馏系统 VAC PVA 节能
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PTA装置醋酸精馏系统共沸剂醋酸正丁酯的回收
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作者 洪作伟 吴廷翰 《金山油化纤》 1990年第1期10-12,共3页
一、概述我厂年产22.5万 t 精对苯二甲酸(PTA)的氧化装置系日本三井油化公司成套引进,是以对二甲苯(PX)为原料,经氧化制得粗对苯二甲酸(CTA),再经加氢精制成精对苯二甲酸。在 PX 氧化过程中,有大量的水生成,并与溶剂醋酸形成稀醋酸溶液... 一、概述我厂年产22.5万 t 精对苯二甲酸(PTA)的氧化装置系日本三井油化公司成套引进,是以对二甲苯(PX)为原料,经氧化制得粗对苯二甲酸(CTA),再经加氢精制成精对苯二甲酸。在 PX 氧化过程中,有大量的水生成,并与溶剂醋酸形成稀醋酸溶液。稀醋酸溶液的分离,是利用共沸剂醋酸正丁酯(NBA)与水形成共沸物,在共沸精馏塔中进行的。而共沸剂 NBA 与水不相溶。 展开更多
关键词 PTA装置 醋酸精馏系统 共沸剂 对苯二甲酸 醋酸正丁酯 回收
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在甲苯/醋酸/水系统中醋酸纤维素的水解
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《精细化工原料及中间体》 2003年第6期42-42,共1页
关键词 甲苯/醋酸/水系统 醋酸纤维素 水解 硫酸 催化剂
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脱乙酸核多糖—醋酸—水系统的相态和流变性能
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作者 Vikhoreva,G.A 《精细化工原料及中间体》 2003年第5期44-44,共1页
关键词 脱乙酸核多糖-醋酸-水系统 相态 流变性能 相对粘度 动态粘度
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PTA装置溶剂脱水系统中共沸剂回收塔的动态模拟及控制
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作者 黄秀辉 王俊 +1 位作者 王应飞 李泽秋 《华东理工大学学报(自然科学版)》 CAS CSCD 北大核心 2018年第4期548-556,共9页
针对以醋酸正丙酯为共沸剂的工业醋酸回收系统中的共沸剂回收塔,基于Aspen Plus和Aspen Dynamics平台在稳态模型的基础上对其进行了动态模拟及动态控制策略研究,设计了两种控制结构并分别对其动态响应特性进行了分析。结果表明,本文方... 针对以醋酸正丙酯为共沸剂的工业醋酸回收系统中的共沸剂回收塔,基于Aspen Plus和Aspen Dynamics平台在稳态模型的基础上对其进行了动态模拟及动态控制策略研究,设计了两种控制结构并分别对其动态响应特性进行了分析。结果表明,本文方法通过直接调节供热流股来控制灵敏板温度具有更好的控制性能,并且能在扰动出现后更快、更稳地达到所需分离要求,回到稳态值、缩短过渡过程并减少相应的物耗及能耗损失,为以后进行共沸剂回收过程的动态实时优化、先进控制等研究以及实现PTA装置的高效优化运行提供有用的理论基础。 展开更多
关键词 醋酸回收系统 共沸剂回收塔 动态模拟 动态控制
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鲁南化工醋酸装置产能提升中的关键核心技术探索
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作者 赵月东 《中氮肥》 CAS 2021年第6期51-54,共4页
当前正值我国醋酸工业发展的关键时期,落后的工艺正在被逐步淘汰,醋酸生产企业只有不断地进行关键核心技术的探索或生产管理精益化,才能在业内保持竞争优势。兖矿鲁南化工有限公司醋酸装置(2套)是我国自主研发的首套甲醇低压羰基合成醋... 当前正值我国醋酸工业发展的关键时期,落后的工艺正在被逐步淘汰,醋酸生产企业只有不断地进行关键核心技术的探索或生产管理精益化,才能在业内保持竞争优势。兖矿鲁南化工有限公司醋酸装置(2套)是我国自主研发的首套甲醇低压羰基合成醋酸工业化装置,2套醋酸装置原设计产能分别为200 kt/a和300 kt/a,近年来鲁南化工立足自身实际,在其醋酸装置产能提升改造过程中持续开展技术攻关和探索,形成了醋酸合成系统新型换热技术、反应釜流体搅拌技术、高速泵国产化等多项关键核心技术,最终实现了醋酸装置总产能成功提升至1000 kt/a、总产能跻身国内前三的目标,稳固了鲁南化工在国内醋酸领域的地位,同时在一定程度上助推了我国醋酸工业的健康可持续发展。 展开更多
关键词 醋酸装置 产能提升 关键核心技术 醋酸合成系统新型换热技术 反应釜流体搅拌技术 高速泵国产化技术 运行状况
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钛在石油化工领域中的应用
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作者 吴以琴 《钛工业进展》 CAS 1991年第1期17-19,共3页
关键词 乙醛系统 醋酸系统 海水换热器
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Research and Implementation of Decreasing the Acetic Acid Consumption in Purified Terephthalic Acid Solvent System 被引量:4
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作者 徐圆 朱群雄 《Chinese Journal of Chemical Engineering》 SCIE EI CAS CSCD 2008年第4期650-655,共6页
Decreasing the acetic acid consumption in purified terephthalic acid (PTA) solvent system has become a hot issue with common concern. In accordance with the technical features, the electrical conductivity is in dire... Decreasing the acetic acid consumption in purified terephthalic acid (PTA) solvent system has become a hot issue with common concern. In accordance with the technical features, the electrical conductivity is in direct proportion to the acetic acid content. General regression neural network (GRNN) is used to establish the model of electrical conductivity on the basis of mechanism analysis, and then particle swarm optimization (PSO) algorithm with the improvement of inertia weight and population diversity is proposed to regulate the operating conditions. Thus, the method of decreasing the acid loss is derived and applied to PTA solvent system in a chemical plant. Cases studies show that the precision of modeling and optimization are higher. The results also provide the optimal operating conditions, which decrease the cost and improve the profit. 展开更多
关键词 acetic acid consumption purified terephthalic acid solvent system general regression neural network particle swarm optimization
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Simulation and Analysis on Multiple Steady States of an Industrial Acetic Acid Dehydration System 被引量:6
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作者 李绍军 黄定伟 《Chinese Journal of Chemical Engineering》 SCIE EI CAS CSCD 2011年第6期983-989,共7页
In this work, an industrial acetic acid dehydration system via heterogeneous azeotropic distillation is simulated by Aspen Plus software. Residue curves are used to analyze the distillating behavior, and appropriate o... In this work, an industrial acetic acid dehydration system via heterogeneous azeotropic distillation is simulated by Aspen Plus software. Residue curves are used to analyze the distillating behavior, and appropriate operating region of the system is determined. Based on steady states simulation, a sensitivity analysis is carried out to detect the output multiple steady states in the system. Different solution branches are observered when the flow rates of the feed stream and the organic reflux stream are selected as manipulated variables. The performance of the column under different steady states is different. A method is oroposed to achieve the desired steady state. 展开更多
关键词 acetic acid dehydration heterogeneous azeotropic distillation residue curve multiple-steady states
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降低VAC和PVA装置醋酸精馏系统能源消耗
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作者 何华祥 《石油和化工节能》 2011年第6期21-23,共3页
分析了四川维尼纶厂VAC和PVA两套生产装置的设计缺陷,并结合这两套独立运行的醋酸精馏系统的特点,将两套生产装置的醋酸精馏系统进行优化整合,同时优化这两套系统的运行方式,并采取措施充分地利用好VAC装置精馏塔出来的精醋酸的热能,从... 分析了四川维尼纶厂VAC和PVA两套生产装置的设计缺陷,并结合这两套独立运行的醋酸精馏系统的特点,将两套生产装置的醋酸精馏系统进行优化整合,同时优化这两套系统的运行方式,并采取措施充分地利用好VAC装置精馏塔出来的精醋酸的热能,从而达到了有效降低单位产品能耗的目的。 展开更多
关键词 优化整合 醋酸精馏系统 VAC PVA 节能
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Vapor-Liquid Equilibrium of Ethyl Acetate+C_nH_(2n+1)OH(n=1,2,3) Binary Systems at 0.3 MPa
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作者 SUSIAL P. RODRIGUEZ-HENRIQUEZ J.J. +1 位作者 SOSA-ROSARIO A. RIOS-SANTANA R. 《Chinese Journal of Chemical Engineering》 SCIE EI CAS CSCD 2012年第4期723-730,共8页
Vapor-liquid equilibrium data for the binary systems of ethyl acetate + methanol,ethyl acetate + ethanol and ethyl acetate + 1-propanol at 0.3 MPa were determined.The experimental data were verified with the point-to-... Vapor-liquid equilibrium data for the binary systems of ethyl acetate + methanol,ethyl acetate + ethanol and ethyl acetate + 1-propanol at 0.3 MPa were determined.The experimental data were verified with the point-to-point test of van Ness(1973).All these systems present an azeotropic point at 0.3 MPa that increases in ester composition for longer alcohol chains.The UNIFAC in different versions and ASOG prediction models were applied. 展开更多
关键词 vapor-liquid equilibrium vapor-liquid equilibrium isobaric data ethyl ester ALCOHOL
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Estrus Grouping in Sheep Treated with Melengestrol Acetate (MGA)
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作者 G. Salas F. Mata +4 位作者 M. Perea R. Garciduefias E. Gutierrez A. Caratachea J. P. Flores 《Journal of Agricultural Science and Technology(A)》 2011年第8期1295-1296,共2页
In Mexico the predominant sheep production system is the semi-extensive with grazing during the day and stanchion afternoon and night. Sheep herd are usually small, approximately 10 to 75 heads. The objectives of thes... In Mexico the predominant sheep production system is the semi-extensive with grazing during the day and stanchion afternoon and night. Sheep herd are usually small, approximately 10 to 75 heads. The objectives of these systems are savings and marketing of lambs. Meat is the main economic product of this kind, the breeding is long, which do not control the delivery dates and ages of the sheep are not uniform, affecting the demand for the local market (for the months of June and December). Therefore the aim of this work was implement a technology that allows the grouping of the estrus and therefore group deliveries for batches of uniform lambs. This technology was designed to suppress the estrus and heifers growth promoter of feedlots, this technology is melengestrol acetate (MGA) which is a synthetic progesterone oral administration that it is easy to manage in the food or alone, economic that it does not represent any risk for sheep females of abortive type, evaluating the effect of the MGA on rate of estrus and gestation in sheep. Work developed in the municipality of Charo from Michoac^in State, M6xico, 20 hair sheep divided in two groups of 10 female, group one treated with MGA and group tow was the whitens. 100% of the sheep treated with a dose of 0.45 mg MGA/head/day for 17 days orally, presented estrus grouped in 5-10 days; however only 50% of the sheep of the witness group presented estrus. In the experimental group there was a rate of 70% with a gestation difference time of no more than ten days gestation and witness group 50%. The MGA is an efficient alternative for the producer of sheep when administered 0.45 mg MGA/head/day for 17 days because inhibits the estrus and once withdrawn treatment manifests estrus synch with which get a rate of gestation elevated by natural riding. 展开更多
关键词 Melengestrol acetate SHEEP ESTRUS PREGNANCY natural riding
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Vapour-Liquid Equilibrium with a New Ebulliometer:Ester+Alcohol System at 0.5 MPa 被引量:2
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作者 P. Susial A. Sosa-Rosario R. Rios-Santana 《Chinese Journal of Chemical Engineering》 SCIE EI CAS CSCD 2010年第6期1000-1007,共8页
A new dynamic ebulliometer is used to determine vapor-liquid equilibrium(VLE) data experimentally. In the equipment,both phases are recirculated. Its operation is a consequence of the Cotrell pump effect produced when... A new dynamic ebulliometer is used to determine vapor-liquid equilibrium(VLE) data experimentally. In the equipment,both phases are recirculated. Its operation is a consequence of the Cotrell pump effect produced when the mixture is heated in a double-walled inverted vessel. The reliability of the apparatus is tested with the mixtures studied previously by various authors. VLE data for the binary systems of methyl acetate + methanol and the methyl acetate + ethanol at 0.5 MPa are determined. The experimental data are confirmed with the point-to-point test of van Ness,applying the Fortran program of Frendslund et al. In addition,the experimental results are com-pared with the UNIFAC(including different versions) and ASOG prediction models. 展开更多
关键词 vapor-liquid equilibrium vapor-liquid equilibrium apparatus vapor pressure ALCOHOL
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Novel Gas-assisted Three-liquid-phase Extraction System for Simultaneous Separation and Concentration of Anthraquinones in Herbal Extract
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作者 杨兴福 梁向峰 +3 位作者 杨良嵘 潘峰 邓伏礼 刘会洲 《Chinese Journal of Chemical Engineering》 SCIE EI CAS CSCD 2014年第9期968-973,共6页
Gas-assisted three-liquid-phase extraction(GATE), which has the advantages of both three-liquid-phase extraction and solvent sublation, is a novel separation technique for separation and concentration of two organic c... Gas-assisted three-liquid-phase extraction(GATE), which has the advantages of both three-liquid-phase extraction and solvent sublation, is a novel separation technique for separation and concentration of two organic compounds into different phases in one step. This highly effective and economically applicable method has been developed for separating emodin and rhein from herbal extract. In a GATE system composed of butyl acetate/PEG4000/ammonium sulfate aqueous solution, influence of various parameters including gas flow rate, flotation time, salt concentration, initial volume of PEG and butyl acetate was investigated. Within 50 min of 30 ml·min-1nitrogen flow, removal ratio of emodin and rhein from aqueous phase could be over 99% and 97%, respectively.Mass fraction of emodin in the BA phase and rhein in the PEG phase could reach 97% and 95%, respectively. It is demonstrated that gas bubbling is effective for partitioning of emodin and rhein into butyl acetate and PEG phase respectively, and dispersed PEG and butyl acetate could be captured from the aqueous solution. Experimental results show that GATE could be an effective and economical technology for concentration and separation of co-existed products in medicinal plants. 展开更多
关键词 Three-liquid-phase extractionGas-assisted solvent extractionSeparationAnthraquinones
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