期刊文献+
共找到746篇文章
< 1 2 38 >
每页显示 20 50 100
Mixing and Vaporization Process of Injecting Water in Hydrogenation Unit 被引量:2
1
作者 Liu Xiaofei Yu Chenyang +3 位作者 Zhu Haiyan Xu Henghui Jin Haozhe Wang Chao 《China Petroleum Processing & Petrochemical Technology》 SCIE CAS 2021年第4期141-150,共10页
Injecting water into the main pipeline is a common method to prevent the ammonium salt corrosion in hydrogenation units.The use of spray nozzle can enhance the effects of washing ammonium salt and reduce the risk of a... Injecting water into the main pipeline is a common method to prevent the ammonium salt corrosion in hydrogenation units.The use of spray nozzle can enhance the effects of washing ammonium salt and reduce the risk of ammonium salt corrosion.The droplet atomization and evaporation model were used to investigate the mixing process of injecting water and gas-oil mixture in a high-pressure environment.The effects of some key parameters including fluid velocity,temperature,and droplet volume fraction on the mixing and vaporization process were analyzed.Numerical simulation results show that with the increase of injecting water flow rate,the fluid velocity increases and the temperature decreases continuously.When the mass flow rate of injecting water is 1.5 t/h,the droplet has the maximum evaporation efficiency and the volume fraction reaches a minimum value.Besides,with the increase of atomization angle and droplet size,the mean velocity and the temperature of fluid decrease continuously.The increase of atomization angle or the decrease of droplet size will accelerate the evaporation process of droplets and reduce the droplet volume fraction,which indicates that the droplet slip velocity and the contact area are the key factors affecting the droplet evaporation rate. 展开更多
关键词 water injection EVAPORATION numerical simulation hydrogenation unit
下载PDF
Evaluation of Vaporized Hydrogen Peroxide Fumigation as a Method for the Bio-decontamination of the High Efficiency Particulate Air Filter Unit 被引量:8
2
作者 JIA Hai Quan LI Yan Ju +6 位作者 SUN Bei ZHAO Si Qing YI Ying ZHAO Ming ZHANG Zong Xing PAN Xin QI Jian Cheng 《Biomedical and Environmental Sciences》 SCIE CAS CSCD 2013年第2期110-117,共8页
Objective To evaluate the performance of vaporized hydrogen peroxide (VHP) for the bio-decontamination of the high efficiency particulate air (HEPA) filter unit. Methods Self-made or commercially available bioindi... Objective To evaluate the performance of vaporized hydrogen peroxide (VHP) for the bio-decontamination of the high efficiency particulate air (HEPA) filter unit. Methods Self-made or commercially available bioindicators were placed at designated locations in the HEPA filter unit under VHP fumigation. The spores on coupons were then extracted by 0.5 h submergence in eluent followed by 200- time violent knocks. Results Due to the presence of HEPA filter in the box, spore recovery from coupons placed at the bottom of the filter downstream was significantly higher than that from coupons placed at the other locations. The gap of decontamination efficiency between the top and the bottom of the filter downstream became narrower with the exposure time extended. The decontamination efficiency of the bottom of the filter downstream only improved gently with the injection rate of H202 increased and the decontamination efficiency decreased instead when the injection rate exceeded 2.5 g/min. The commercially available bioindicators were competent to indicate the disinfection efficiency of VHP for the HEPA filter unit. Conclusion The HEPA filter unit is more difficult than common enclosure to decontaminate using VHP fumigation. Complete decontamination can be achieved by extending fumigation time. VHP fumigation can be applied for in-situ biodecontamination of the HEPA filter unit as an alternative method to formaldehyde fumigation. 展开更多
关键词 Vaporized hydrogen peroxide FUMIGATION Bio-decontamination High efficiency particulateair filter unit Spore killing
下载PDF
The Use of Hydrogen as a Fuel for Inland Waterway Units 被引量:3
3
作者 M. Morsy El Gohary Yousri M. A. Welaya AmrAbdelwahabSaad 《Journal of Marine Science and Application》 2014年第2期212-217,共6页
Escalating apprehension about the harmful effects of widespread use of conventional fossil fuels in the marine field and in internal combustion engines in general, has led to a vast amount of efforts and the directing... Escalating apprehension about the harmful effects of widespread use of conventional fossil fuels in the marine field and in internal combustion engines in general, has led to a vast amount of efforts and the directing of large capital investment towards research and development of sustainable alternative energy sources. One of the most promising and abundant of these sources is hydrogen. Firstly, the use of current fossil fuels is. discussed focusing on the emissions and economic sides to emphasize the need for a new, cleaner and renewable fuel with particular reference to hydrogen as a suitable possible alternative. Hydrogen properties, production and storage methods are then reviewed along with its suitability from the economical point of view. Finally, a cost analysis for the use of hydrogen in internal combustion engines is carried out to illustrate the benefits of its use as a replacement for diesel. The outcome of this cost analysis shows that 98% of the capital expenditure is consumed by the equipment, and 68.3% of the total cost of the equipment is spent on the solar photovoltaic cells. The hydrogen plant is classified as a large investment project because of its high initial cost which is about 1 billion US$; but this is justified because hydrogen is produced in a totally green way. When hydrogen is used as a fuel, no harmful emissions are obtained. 展开更多
关键词 sustainable alternative energy sources hydrogen fuel hydrogen properties hydrogen production hydrogen storage costanalysis inland waterway units
下载PDF
Application of Resid Hydrogenation Process in China's Mainland 被引量:1
4
作者 Diao Wangsheng 《China Petroleum Processing & Petrochemical Technology》 SCIE CAS 2007年第1期7-12,共6页
This article mainly refers to a brief introduction on the design and operation of resid hydrogenation units in China's Mainland in order to keep the peers abreast of the basic status of aoolication of resid hydrog... This article mainly refers to a brief introduction on the design and operation of resid hydrogenation units in China's Mainland in order to keep the peers abreast of the basic status of aoolication of resid hydrogenation process in the China's Mainland. 展开更多
关键词 resid hydrogenation process unit design conditions production and operation
下载PDF
STUDY ON MAXIMUM HYDROGEN CAPACITY FOR Zr-Ni AMORPHOUS ALLOY
5
作者 张东明 《Journal of Wuhan University of Technology(Materials Science)》 SCIE EI CAS 2000年第4期28-32,共5页
To design the amorphous hydrogen storage alloy efficiently, the maximum hydrogen capacities for Zr - Ni amorphous alloy were calculated. Based on the Rhomb Unit Structure Model(RUSM) for amorphous alloy and the experi... To design the amorphous hydrogen storage alloy efficiently, the maximum hydrogen capacities for Zr - Ni amorphous alloy were calculated. Based on the Rhomb Unit Structure Model(RUSM) for amorphous alloy and the experimental result that hydrogen atoms exist in 3Zr1Ni and 4Zr tetrahedron interstices in Zr-Ni amolphous alloy, the numbers of 3Zr-1Ni and 4Zr tetrahedron interstices in a RUSM were calculated which correspond to the hydrogen capacity. The two extremum Zr distribution states were calculated, such as highly heterogeneous Zr distribution and homogeneous Zr distribution. The calculated curves of hydrogen capacity with different Zr contents at two states indicate that the hydrogen capacity increases with increasing Zr content and reaches its maximum when Zr is 75%. The theoretical maximum hydrogen capacity for Zr - Ni amorphous alloy is 2.0 (H/M). Meanwhile, the hydrogen capacity of heterogenous Zr distribution alloy is higher than that of homogenous one at the same Zr content. The experimental results prove the calculated results reasonable, and accordingly, the experimental results that the distribution of Zr atom in amorphous alloy occur heterogeneous after a few hydrogen absorption desorption cycles can be explained. 展开更多
关键词 Rhomb unit Structure Model (RUSM) 3Zr1Ni or 4Zr tetrahedron interstice maximum hydrogen capacity
下载PDF
Corrosion Behaviors of Disinfectants on Dental Unit Waterlines
6
作者 张玲 QIU Jiajun +1 位作者 邢敏 钱文昊 《Journal of Wuhan University of Technology(Materials Science)》 SCIE EI CAS CSCD 2023年第4期938-941,共4页
To investigate the corrosion behaviors and antibacterial effects of sodium hypochlorite(NaClO)and hydrogen peroxide silver ion(HPSI)disinfectants with different concentrations against dental unit waterlines and provid... To investigate the corrosion behaviors and antibacterial effects of sodium hypochlorite(NaClO)and hydrogen peroxide silver ion(HPSI)disinfectants with different concentrations against dental unit waterlines and provide guidance and reference for the use of chemical disinfectants,polyurethane tubes were immersed in ultrapure water(control group),0.1%NaClO,0.5%NaClO,1.0%NaClO,2.5%HPSI,5.0%HPSI,and 10%HPSI solutions for 6,12,and 18 weeks.Contact angles and Fourier transform infrared spectra were detected.Surface morphologies were observed using scanning electron microscopy and antibacterial activity was evaluated using Gram-positive Staphylococcus aureus(S.aureus).The results showed that sodium hypochlorite and hydrogen peroxide silver ion disinfectants presented good antibacterial activity against S.aureus.However,sodium hypochlorite could cause serious damage to the water pipes where corrosion pits and cracks were observed,and increasing the concentration of sodium hypochlorite could accelerate the corrosion process.Hydrogen peroxide silver ion disinfectants had no obvious damage to the water pipes.Therefore,hydrogen peroxide silver ion disinfectants are recommended to use for controlling bacterial infection in dental unit waterlines which can reduce the damage to the water pipes. 展开更多
关键词 DISINFECTANT dental unit waterlines sodium hypochlorite hydrogen peroxide silver ion
下载PDF
Study and Strategy on Expansion of Steam Cracking Unit to 650 kt/a at Yanshan Petrochemical Company
7
作者 Cao Xianghong (SINOPEC, Beijing 100011) 《工程科学(英文版)》 2003年第2期1-12,共12页
After having expanded its capacity from 300 kt/a to 450 kt/a in 1994, the steam cracking unit of Yanshan Petrochemical Company was still experiencing such problems as low feedstock flexibility, high energy consumption... After having expanded its capacity from 300 kt/a to 450 kt/a in 1994, the steam cracking unit of Yanshan Petrochemical Company was still experiencing such problems as low feedstock flexibility, high energy consumption and smaller production capacity as compared to other ethylene units constructed in the same time. In order to fully improve technical capability, reduce energy consumption, improve feedstock flexibility and increase production capacity of steam crackers, a lot of technical transform schemes on steam cracking were studied and compared with attention focused on the feasibility, safety, operability of the related revamp schemes, as well as the advanced nature and economical features. The transform scheme decided includes following projects. For the pyrolysis quench compression system, the pyrolysis gasoline fractionation tower is retrofitted on the site, quench water tower, pyrolysis gas compressor and steam turbine are replaced by new ones respectively. For the separation system a low pressure methane removal technology is adopted with the demethanizer tower replaced, coupled with the C 3 catalytic rectification/hydrogenation technology, while the high pressure depropanizer is replaced with addition of a propylene rectification tower. The fractionation flow sheet and equipment are adjusted with addition of a propylene compressor and compressor for binary mixture of methane ethylene cooling agents. The revamped complex has expanded the ethylene capacity to the target of 660 kt/a with the actual capacity reaching 710 kt/a, remarkably reduced the energy consumption, and is capable of using naphtha, light diesel fuel, heavy diesel fuel and the hydrocracked tail oil as the steam cracking feedstock. This project is the first to apply refrigeration by means of a mixed cooling agent and has succeeded in using C\-3 catalytic rectification/hydrogenation technology, which has given an impetus to the progress of steam cracking industry in the world. 展开更多
关键词 EXPANSION steam CRACKING unit binary mixed cooling agent catalytic RECTIFICATION hydrogenation technology
下载PDF
固体氧化物电解槽辅助煤电机组深度调峰技术可行性研究 被引量:2
8
作者 王林 刘晓莎 +3 位作者 胡平 李治宽 李昭 张鹏 《热力发电》 CAS CSCD 北大核心 2024年第2期133-141,共9页
常规的煤电机组灵活性改造方案,难以消除频繁快速变负荷对热力系统造成的潜在寿命折损与设备安全风险。为提高煤电机组参与深度调峰的长期安全性与经济性,以某国产超超临界二次再热1000 MW燃煤机组为应用对象,提出了基于氢储能系统的煤... 常规的煤电机组灵活性改造方案,难以消除频繁快速变负荷对热力系统造成的潜在寿命折损与设备安全风险。为提高煤电机组参与深度调峰的长期安全性与经济性,以某国产超超临界二次再热1000 MW燃煤机组为应用对象,提出了基于氢储能系统的煤电机组“健康调峰”技术路线,并论证了调峰煤电制氢的间接碳减排意义。在此基础上,分析比较了不同制氢工艺与煤电厂生产条件的匹配程度,认为固体氧化物电解槽(SOEC)制氢为综合最优方案,据此给出了SOEC耦合煤电调峰的原理性设计方案,最后以年度负荷曲线对新方案进行了财务分析。计算结果表明,示例机组自第6年起每年可获得1.07亿元/年的净利润,每年减少碳排放281.92 t,同时获得设备延寿、降耗减碳等其他收益。相关结论对于指导调峰煤电机组的健康安全运行具有参考意义。 展开更多
关键词 电解制氢 固体氧化物电解槽 煤电机组 可行性 财务分析
下载PDF
面向灵活性挖掘的电-氢混联综合能源系统机组组合研究
9
作者 陈胜 陈明健 +3 位作者 卫志农 周亦洲 韩海腾 孙国强 《电网技术》 EI CSCD 北大核心 2024年第11期4473-4481,I0017-I0019,I0015,共13页
随着电制氢技术的逐步成熟,利用新能源制氢与管道输氢有望为能源系统的深度脱碳提供重要支撑。该文提出了电-氢耦合综合能源系统机组组合模型,考虑了发电机组与电解制氢系统协同提供灵活运行备用。首先通过高斯混合模型得到新能源预测... 随着电制氢技术的逐步成熟,利用新能源制氢与管道输氢有望为能源系统的深度脱碳提供重要支撑。该文提出了电-氢耦合综合能源系统机组组合模型,考虑了发电机组与电解制氢系统协同提供灵活运行备用。首先通过高斯混合模型得到新能源预测误差分布,获取其95%置信区间,确定新能源电力系统灵活备用需求;其次提出了考虑灵活备用的电-氢混联综合能源系统机组组合模型,计及了电解制氢系统三状态(开机、关机、热备用)灵活运行模型;算例分析验证了所提电制氢三状态机组组合模型的有效性,分析了新能源渗透率对制氢量与节点电价的影响。 展开更多
关键词 电-氢混联综合能源系统 绿氢 机组组合 灵活性挖掘
下载PDF
基于氢储能的煤电机组灵活性改造方案研究
10
作者 王林 刘晓莎 +2 位作者 胡平 李昭 张鹏 《工业加热》 CAS 2024年第4期63-67,共5页
现有的煤电机组灵活性改造方案,聚焦局部与短期,难以消除频繁快速变负荷对热力系统造成的长期寿命折损与安全风险。为提高煤电机组参与电力市场辅助服务的安全性与经济性,提出建立基于氢储能系统的煤电机组系统级灵活性改造方案。分析... 现有的煤电机组灵活性改造方案,聚焦局部与短期,难以消除频繁快速变负荷对热力系统造成的长期寿命折损与安全风险。为提高煤电机组参与电力市场辅助服务的安全性与经济性,提出建立基于氢储能系统的煤电机组系统级灵活性改造方案。分析了现有制氢路线,认为固体氧化物电解槽路线与煤电机组结合度高,且具有辅助煤电机组削减碳排放、提升经营收益的综合优点。以某国产1000 MW超超临界二次再热燃煤机组为应用对象,提出了氢储能系统与煤电机组的可行性结合方案。相关研究成果对于开发新型系统级的安全、健康经济的煤电灵活性提升改造方案具有参考意义。 展开更多
关键词 氢储能 固体氧化物电解槽 煤电机组 灵活性 安全健康
下载PDF
基于ASPEN软件的戊烷发泡剂生产实践及增产措施
11
作者 穆海涛 刘春柳 《石油炼制与化工》 CAS CSCD 北大核心 2024年第3期61-66,共6页
炼化企业中,戊烷发泡剂可以利用预加氢装置拔出的轻石脑油组分进行生产,而国家标准GB T 22053—2020对发泡剂质量要求更加严格。通过构建预加氢装置汽提塔、分馏塔及脱戊烷塔的ASPEN PLUS模型,对戊烷发泡剂生产流程的控制参数进行分析测... 炼化企业中,戊烷发泡剂可以利用预加氢装置拔出的轻石脑油组分进行生产,而国家标准GB T 22053—2020对发泡剂质量要求更加严格。通过构建预加氢装置汽提塔、分馏塔及脱戊烷塔的ASPEN PLUS模型,对戊烷发泡剂生产流程的控制参数进行分析测算,制定了生产调整方案。工业试验结果表明:戊烷发泡剂组成与脱戊烷塔塔顶灵敏板温度密切相关,保证塔顶发泡剂组分质量分数差值范围为±2%,其塔顶温度变化需控制±0.3℃。同时,从汽提塔操作、产品牌号、加工原油种类等方面入手,对戊烷发泡剂增产效果进行分析,提高企业的经济效益。 展开更多
关键词 预加氢装置 汽提塔 戊烷 发泡剂 灵敏板温度
下载PDF
半再生重整装置催化剂硅中毒现象及分析
12
作者 王辉 常永胜 徐洪君 《炼油技术与工程》 CAS 2024年第1期36-41,共6页
某炼油企业的半再生重整装置因重整催化剂活性下降而停工,更换了第一反应器和第二反应器的催化剂。对旧催化剂进行分析后发现,第一反应器催化剂二氧化硅质量分数高达20.40%,因此判断重整催化剂发生了硅中毒。在硅中毒期间:第一反应器的... 某炼油企业的半再生重整装置因重整催化剂活性下降而停工,更换了第一反应器和第二反应器的催化剂。对旧催化剂进行分析后发现,第一反应器催化剂二氧化硅质量分数高达20.40%,因此判断重整催化剂发生了硅中毒。在硅中毒期间:第一反应器的温降由初期的73.70℃下降到末期的20.12℃,重整反应后移到第二反应器;循环氢的氢气纯度上升到90%,纯氢产率下降到2.17%;稳定汽油RON(研究法辛烷值)下降到83.7。重整催化剂硅中毒较为罕见,其表现与氮中毒相似,容易误判为催化剂氮中毒。对硅进行溯源,确认是原油携带。分析认为:重整预加氢捕硅剂无法完全捕获所有硅,导致部分硅穿透预加氢系统;硅对预加氢催化剂的影响小于对重整催化剂的影响;硅中毒会导致催化剂的氯流失,需要加大注氯量。 展开更多
关键词 半再生重整装置 催化剂 硅中毒 反应温降 循环氢组分 稳定汽油 原料硅含量
下载PDF
美、韩两国氢能法律制度比较研究
13
作者 董溯战 经天逸 《中国石油大学学报(社会科学版)》 2024年第6期46-56,共11页
中国能源结构清洁转型需要氢能革命,而氢能革命应以法律革命为保障。中国氢能产业虽已呈现出快速发展之势,但法律制度的缺位成为重要的阻却因素。美、韩两国业已构筑了体现本国国情的规范氢能产业发展的法律制度,两国氢能法的理念和制... 中国能源结构清洁转型需要氢能革命,而氢能革命应以法律革命为保障。中国氢能产业虽已呈现出快速发展之势,但法律制度的缺位成为重要的阻却因素。美、韩两国业已构筑了体现本国国情的规范氢能产业发展的法律制度,两国氢能法的理念和制度安排皆有诸多可借鉴之处。在分析比较美、韩两国氢能法律制度的基础上,中国可借鉴美韩经验选择适当立法模式,构建涵盖管理体制、规划、发展激励和安全监管的氢能规则,为中国氢能发展提供制度保障。 展开更多
关键词 美国 韩国 氢能 法律制度 比较
下载PDF
大型硫回收装置多功能CO变换加氢催化剂应用总结
14
作者 裴爱霞 《炼油技术与工程》 CAS 2024年第5期53-56,共4页
普光气田是国内成功开发的首个高含硫气田,原料气(天然气)碳硫比高,再生酸性气CO_(2)含量高,会反应生成CO继而生成COS、CS_(2)等有机物,成为影响装置达标排放的关键因素之一。研究开发了具有CO变换功能的克劳斯尾气加氢催化剂,并成功应... 普光气田是国内成功开发的首个高含硫气田,原料气(天然气)碳硫比高,再生酸性气CO_(2)含量高,会反应生成CO继而生成COS、CS_(2)等有机物,成为影响装置达标排放的关键因素之一。研究开发了具有CO变换功能的克劳斯尾气加氢催化剂,并成功应用于中国石化中原油田普光气田天然气净化厂200 kt/a硫回收装置。工业应用结果表明:加氢反应器过程气CO变换率超过90%,在线炉制氢天然气消耗量减少279 m^(3)/h,催化剂加氢转化率、有机硫水解率均超过99%,烟气SO_(2)排放浓度降至200 mg/m^(3)以下,CO排放浓度降低了90%,效益显著。 展开更多
关键词 硫回收装置 多功能 CO变换 加氢催化剂 反应温度 反应空速 活性 有机硫
下载PDF
计及氢储能-制氨-碳捕集的综合能源系统低碳优化调度
15
作者 梁俊鹏 张高航 +2 位作者 李凤婷 解超 王婷 《电力自动化设备》 EI CSCD 北大核心 2024年第10期16-23,共8页
针对高风光渗透率的综合能源系统存在的弃能及备用压力问题,考虑氢能单元、碳捕集和制氨装置联合运行,提出了一种含氢能、氨能与碳捕集的综合能源系统低碳优化调度方法,以提升系统的风光消纳能力和运行灵活性。一方面,提出了综合能源系... 针对高风光渗透率的综合能源系统存在的弃能及备用压力问题,考虑氢能单元、碳捕集和制氨装置联合运行,提出了一种含氢能、氨能与碳捕集的综合能源系统低碳优化调度方法,以提升系统的风光消纳能力和运行灵活性。一方面,提出了综合能源系统的运行框架,分析了氢能单元、制氨装置和火电机组掺氨燃烧以及碳捕集装置参与消纳风光的灵活经济运行策略,并进行了机理分析与建模;另一方面,为了缓解系统备用压力,建立了氢能单元-碳捕集-火电协同备用优化模型,挖掘氢能单元与碳捕集装置的备用能力,进而以总运行成本最小为目标,建立了综合能源系统的低碳经济调度模型。基于改进的IEEE 39节点系统进行仿真分析,结果验证了所提调度方法的有效性和可行性。 展开更多
关键词 综合能源系统 低碳调度 氢能单元 氢-氨利用 碳捕集 备用优化
下载PDF
浆态床重石脑油加工路线的模拟优化及应用 被引量:1
16
作者 许绍东 代恩东 +5 位作者 魏文 刘亭亭 高伟 崔登科 毛玲娟 李伟龙 《石化技术与应用》 CAS 2024年第3期205-208,共4页
利用英国KBC公司开发的NHTR-SIM和HCR-SIM流程模拟软件分别模拟优化了石脑油加氢装置和柴油加氢裂化装置的加工全流程,提出了将浆态床重石脑油由全部掺炼于350万t/a柴油加氢裂化装置改为全部掺炼于360万t/a石脑油加氢装置,再进入连续重... 利用英国KBC公司开发的NHTR-SIM和HCR-SIM流程模拟软件分别模拟优化了石脑油加氢装置和柴油加氢裂化装置的加工全流程,提出了将浆态床重石脑油由全部掺炼于350万t/a柴油加氢裂化装置改为全部掺炼于360万t/a石脑油加氢装置,再进入连续重整装置的加工优化方案。结果表明:在模拟石脑油加氢装置掺炼浆态床重石脑油时,产品精制重石脑油的含硫、氮量分别为0.37,0.42μg/g,均满足重整装置进料小于0.5μg/g的指标要求,该方案可行;优化实施后,虽然该方案仅协同运行半年多,共加工浆态床重石脑油20.47万t,促进柴油组分原料加工量提升了17.82万t,但为公司2022年度综合创效达7928.3万元。 展开更多
关键词 浆态床渣油加氢装置 重石脑油 石脑油加氢装置 柴油加氢裂化装置 模拟优化
下载PDF
大型天然气净化厂硫磺回收装置二氧化硫控制技术研究 被引量:2
17
作者 胡海光 《辽宁化工》 CAS 2024年第2期317-319,共3页
硫磺回收装置是化工企业处理酸性气的关键装置,也是控制尾气二氧化硫的重要环节。以西南地区2个特大化工企业为例,介绍硫磺回收装置的工艺流程,对比分析其技术特点,梳理2017—2022年相关文献,分析得出硫磺回收装置二氧化硫控制措施,从... 硫磺回收装置是化工企业处理酸性气的关键装置,也是控制尾气二氧化硫的重要环节。以西南地区2个特大化工企业为例,介绍硫磺回收装置的工艺流程,对比分析其技术特点,梳理2017—2022年相关文献,分析得出硫磺回收装置二氧化硫控制措施,从参数优化、材质升级、应急处置培训3个方面提出攻关方向。结果表明:控制酸性气与燃烧空气比值稳定是工艺调整主攻方向,液硫池废气治理改造减排效果显著,并在行业内逐步推广。 展开更多
关键词 硫磺回收装置 二氧化硫 硫化氢
下载PDF
“双碳”目标下我国能源电力系统发展趋势分析:绿电替代与绿氢替代 被引量:1
18
作者 周孝信 赵强 +1 位作者 张玉琼 杨宏华 《中国电机工程学报》 EI CSCD 北大核心 2024年第17期6707-6720,I0003,共15页
能源电力系统的低碳转型是实现碳达峰碳中和目标的关键所在。为研判“双碳”目标下我国能源电力系统的未来发展趋势,该文构建了考虑绿电替代与绿氢替代的中长期能源电力发展估算模型,基于模型对2020—2060年我国能源电力发展场景进行测... 能源电力系统的低碳转型是实现碳达峰碳中和目标的关键所在。为研判“双碳”目标下我国能源电力系统的未来发展趋势,该文构建了考虑绿电替代与绿氢替代的中长期能源电力发展估算模型,基于模型对2020—2060年我国能源电力发展场景进行测算,分析相关核心指标的演化趋势,并针对绿电绿氢与现有能源系统协同发展的多能互补综合能源发展模式提出方案设想。结果表明,以绿电为主、绿氢为辅对传统化石能源的“双替代”,作为实现“双碳”目标的关键措施,将在新型能源体系和新型电力系统建设中发挥决定性作用,分别针对源端能源生产基地和终端消费区域提出的综合能源生产单元(integrated energy production unit,IEPU)和综合能源产消单元(integrated energy production and consumption unit,IECU)设想,可为促进多类型资源协同优化和高效配置、支撑构建新型能源体系与新型电力系统提供方案参考。 展开更多
关键词 绿电替代 绿氢替代 能源电力系统 发展趋势 综合能源生产单元 综合能源产消单元
下载PDF
柴油加氢装置柴油产品硫、芳烃含量超标原因探讨
19
作者 刘传琦 郭洋 许红香 《当代石油石化》 CAS 2024年第4期45-49,共5页
石油燃料的使用是导致大气污染的主要原因,而柴油中的硫、芳烃含量是影响污染的关键因素。柴油加氢装置生产运行至末期时,随着原料油性质、加工负荷、催化剂性能、生产方案、操作工况等条件的变化,装置中柴油产品硫、芳烃含量会出现超... 石油燃料的使用是导致大气污染的主要原因,而柴油中的硫、芳烃含量是影响污染的关键因素。柴油加氢装置生产运行至末期时,随着原料油性质、加工负荷、催化剂性能、生产方案、操作工况等条件的变化,装置中柴油产品硫、芳烃含量会出现超标现象,通过调整原料配比及性质、优化生产方案等方式,可实现对柴油加氢装置柴油产品硫、芳烃含量超标现象的有效控制,为同类生产装置提供借鉴。 展开更多
关键词 柴油加氢装置 柴油 硫含量 芳烃含量
下载PDF
加氢装置循环氢脱硫塔腐蚀分析
20
作者 夏永生 张磊 +2 位作者 苗普 张宏飞 于凤昌 《石油化工腐蚀与防护》 CAS 2024年第5期25-31,共7页
加氢过程对提高原油加工深度、产品质量和生产效率至关重要,但加氢生成的H_(2)S会导致后序管道设备产生腐蚀以及循环氢中的氢分压降低,为此常需设置循环氢脱硫塔来脱除循环氢中的H_(2)S。循环氢脱硫塔中存在多种腐蚀介质和腐蚀风险,该... 加氢过程对提高原油加工深度、产品质量和生产效率至关重要,但加氢生成的H_(2)S会导致后序管道设备产生腐蚀以及循环氢中的氢分压降低,为此常需设置循环氢脱硫塔来脱除循环氢中的H_(2)S。循环氢脱硫塔中存在多种腐蚀介质和腐蚀风险,该文结合加氢装置工艺特点对循环氢脱硫塔中的腐蚀类型、影响因素和腐蚀控制措施进行了分析和讨论,对某企业渣油加氢装置循环氢脱硫塔现场勘验后发现的腐蚀问题,也进行了分析论证,提出了腐蚀防控措施,从而为加氢装置的安全运行提供了借鉴和技术支撑。 展开更多
关键词 加氢装置 循环氢脱硫塔 腐蚀分析 腐蚀防控
下载PDF
上一页 1 2 38 下一页 到第
使用帮助 返回顶部