
浏览全部资源
扫码关注微信
1.中国石油工程建设有限公司华北分公司,河北 任丘 062550
2.中国石油宝鸡石油机械有限责任公司河北钻采装备制造分公司,河北 任丘 062550
3.北京石油化工学院 能源工程系,北京 102600
张天娇(1987—),硕士,工程师,研究方向为CCUS及新能源技术,E-mail:ztj201307@126.com。
收稿:2025-05-30,
修回:2025-08-25,
纸质出版:2025-10-25
移动端阅览
张天娇,刘永铎,刘欣等.新型双塔吸收半贫液脱碳工艺模拟与分析[J].低碳化学与化工,2025,50(10):138-144.
ZHANG Tianjiao,LIU Yongduo,LIU Xin,et al.Simulation and analysis of novel dual-tower absorption semi-lean liquid decarbonization process[J].Low-Carbon Chemistry and Chemical Engineering,2025,50(10):138-144.
张天娇,刘永铎,刘欣等.新型双塔吸收半贫液脱碳工艺模拟与分析[J].低碳化学与化工,2025,50(10):138-144. DOI: 10.12434/j.issn.2097-2547.20250198.
ZHANG Tianjiao,LIU Yongduo,LIU Xin,et al.Simulation and analysis of novel dual-tower absorption semi-lean liquid decarbonization process[J].Low-Carbon Chemistry and Chemical Engineering,2025,50(10):138-144. DOI: 10.12434/j.issn.2097-2547.20250198.
对于高含CO
2
天然气脱碳,常规的半贫液脱碳工艺存在脱碳深度不足、再生能耗过高等问题。为提高脱碳精度、降低再生能耗,提出了一种新型双塔吸收半贫液脱碳工艺。利用Aspen HYSYS软件建立了新工艺流程模型,采用单因素敏感性分析,研究了胺液循环量、半贫液分流比和再生温度等关键参数对脱碳效果及再生能耗的影响,并进行了参数优化。在最优工艺参数(原料气CO
2
体积分数为23.5%时,胺液循环量为1195 m
3
/h
,半贫液分流比为75%,再生温度为120 ℃)下,将新工艺与常规工艺进行了对比。结果表明,相比常规工艺,新工艺净化气流量增大了21.63 × 10
4
m
3
/d,折合经济效益为59.05 × 10
4
CNY/d;吸收塔、再生塔及富液闪蒸罐等装置的尺寸均大幅度减小;新工艺再生能耗和冷却能耗分别降低了4.836%和4.572%,节能效果明显。
For the decarbonization of high CO
2
content natural gas
the conventional semi-lean liquid process suffers from insufficient decarbonization depth and excessively high regeneration energy consumption. To improve decarbonization accuracy and reduce regeneration energy consumption
a novel dual-tower absorption semi-lean liquid decarbonization process was proposed. A process model of the new scheme was established using Aspen HYSYS software
and a single-factor sensitivity analysis was conducted to investigate the effects of key parameters
including amine liquid circulation rate
semi-lean liquid split ratio and regeneration temperature
on decarbonization performance and regeneration energy consumption
followed by parameter optimization. Under the optimal process conditions (raw gas with CO
2
volume fraction of 23.5%
amine liquid circulation rate of 1195 m
3
/h
semi-lean liquid split ratio of 75% and regeneration temperature of 120 ℃)
the new process was compared with the conventional process. The results show that
compared with the conventional process
the new process increases the purified gas flow by 21.63 × 10
4
m
3
/d
corresponding to an economic benefit of 59.05 × 10
4
CNY/d. Moreover
the sizes of the absorption tower
regeneration tower and rich liquid flash tank are all significantly reduced. The regeneration and cooling energy consumption of the new process are reduced by 4.836% and 4.572%
respectively
demonstrating a notable energy-saving effect.
邹才能 , 林敏捷 , 马锋 , 等 . 碳中和目标下中国天然气工业进展、挑战及对策 [J ] . 石油勘探与开发 , 2024 , 51 ( 2 ): 1 - 17 .
ZOU C N , LIN M J , MA F , et al . Development, challenges and strategies of natural gas industry under carbon neutral target in China [J ] . Petroleum Exploration and Development , 2024 , 51 ( 2 ): 1 - 17 .
马国光 , 王金阳 , 张涛 . 二氧化碳捕集耦合工艺设计与优化 [J ] . 低碳化学与化工 , 2024 , 49 ( 7 ): 80 - 87 .
MA G G , WANG J Y , ZHANG T . Design and optimization of CO 2 capture coupled process [J ] . Low-Carbon Chemistry and Chemical Engineering , 2024 , 49 ( 7 ): 80 - 87 .
LIU Z , DENG Z , DAVIS S , et al . Monitoring global carbon emissions in 2022 [J ] . Nature Reviews Earth & Environment , 2023 , 4 ( 4 ): 205 - 206 .
王剑琨 , 张媛媛 , 唐建峰 , 等 . 天然气脱碳胺液再生能耗分析 [J ] . 天然气化工—C1化学与化工 , 2022 , 47 ( 1 ): 113 - 118 .
WANG J K , ZHANG Y Y , TANG J F , et al . Analysis of energy consumption of amine solution regeneration in natural gas decarburized [J ] . Natural Gas Chemical Industry , 2022 , 47 ( 1 ): 113 - 118 .
张天娇 , 刘欣 , 刘永铎 . 1000 × 10 4 m 3 /d天然气碳捕集工艺方案优选 [J ] . 现代化工 , 2024 , 44 ( 11 ): 229 - 233 .
ZHANG T J , LIU X , LIU Y D . Research on CO 2 capture technology of 1000 × 10 4 m 3 /d natural gas [J ] . Modern Chemical Industry , 2024 , 44 ( 11 ): 229 - 233 .
洪宗平 , 叶楚梅 , 吴洪 , 等 . 天然气脱碳技术研究进展 [J ] . 化工学报 , 2021 , 72 ( 12 ): 6030 - 6048 .
HONG Z P , YE C M , WU H , et al . Research progress in CO 2 removal technology of natural gas [J ] . CIESC Journal , 2021 , 72 ( 12 ): 6030 - 6048 .
韩伟刚 . 天然气脱除二氧化碳技术的研究 [J ] . 辽宁化工 , 2023 , 52 ( 3 ): 420 - 422+429 .
HAN W G . Research on natural gas carbon dioxide removal technology [J ] . Liaoning Chemical Industry , 2023 , 52 ( 3 ): 420 - 422+429 .
张天娇 , 刘欣 , 张青 , 等 . 基于HYSYS模拟的低浓度CO 2 捕集配方优选及参数优化 [J ] . 当代化工 , 2024 , 59 ( 9 ): 31 - 36 .
ZHANG T J , LIU X , ZHANG Q , et al . Formula and parameters optimization of low concentration CO 2 capture based on HYSYS simulation [J ] . Contemporary Chemical Industry , 2024 , 59 ( 9 ): 31 - 36 .
王开岳 . 天然气净化工艺 [M ] . 北京 : 石油工业出版社 , 2015 : 16 - 54 .
WANG K Y . Natural gas purification process [M ] . Beijing : Petroleum Industry Press , 2015 : 16 - 54 .
蔡勇 , 朱瑞松 , 魏弢 , 等 . 二氧化碳捕集技术研究进展及其在驱油中的应用 [J ] . 低碳化学与化工 , 2024 , 49 ( 1 ): 85 - 93 .
CAI Y , ZHU R S , WEI T , et al . Research progress of carbon dioxide capture technologies and their application in enhanced oil recovery [J ] . Low-Carbon Chemistry and Chemical Engineering , 2024 , 49 ( 1 ): 85 - 93 .
邵青楠 , 顾鑫诚 , 邓春 , 等 . 天然气处理工艺建模与模拟进展 [J ] . 石油科学通报 , 2019 , 4 ( 2 ): 192 - 203 .
SHAO Q N , GU X C , DENG C , et al . Research advances in the simulation and modeling of natural gas treatment process [J ] . Petroleum Science Bulletin , 2019 , 4 ( 2 ): 192 - 203 .
唐建峰 , 刘云飞 , 张媛媛 , 等 . 半贫液工艺再生过程闪蒸及能耗模拟优化 [J ] . 石油学报(石油加工) , 2021 , 37 ( 5 ): 1050 - 1059 .
TANG J F , LIU Y F , ZHANG Y Y , et al . Simulation optimization on flash evaporation and energy consumption during regeneration of semi-lean solution process [J ] . ACTA Petrolei Sinica (Petroleum Processing Section) , 2021 , 37 ( 5 ): 1050 - 1059 .
花亦怀 , 刘倩玉 , 丁御 , 等 . 哌嗪活化N-甲基二乙醇胺半贫液脱碳工艺配方优选及参数优化 [J ] . 石油学报(石油加工) , 2020 , 36 ( 4 ): 812 - 822 .
HUA Y H , LIU Q Y , DING Y , et al . Formula and process parameters optimization of PZ-activated MDEA semi-lean solution decarburization process [J ] . ACTA Petrolei Sinica (Petroleum Processing Section) , 2020 , 36 ( 4 ): 812 - 822 .
张天娇 , 刘欣 , 刘永铎 , 等 . 分流吸收-级间循环冷却耦合脱碳工艺研究 [J ] . 现代化工 , 2024 , 44 ( 12 ): 1 - 7 .
ZHANG T J , LIU X , LIU Y D , et al . Study on the coupled decarbonization process of shunt absorption-interstage recirculation cooling [J ] . Modern Chemical Industry , 2024 , 44 ( 12 ): 1 - 7 .
李浩玉 , 蒋洪 , 胡成星 , 等 . 天然气半贫液脱碳工艺换热网络优化 [J ] . 天然气化工—C1化学与化工 , 2021 , 46 ( 1 ): 85 - 89 .
LI H Y , JIANG H , HU C X , et al . Optimization of heat exchange network of natural gas semi-lean liquid decarbonization process [J ] . Natural Gas Chemical Industry , 2021 , 46 ( 1 ): 85 - 89 .
范明龙 , 花亦怀 , 苏清博 . 高含CO 2 天然气胺法脱碳工艺设计 [J ] . 石油与天然气化工 , 2021 , 50 ( 2 ): 39 - 45 .
FAN M L , HUA Y H , SU Q B . Design of amine decarbonization process for high CO 2 content natural gas [J ] . Chemical Engineering of Oil & Gas , 2021 , 50 ( 2 ): 39 - 45 .
阮洪江 , 张乔良 , 刘峰 , 等 . 多孔介质中CO 2 埋存机理物理模拟实验评价 [J ] . 辽宁石油化工大学学报 , 2024 , 44 ( 2 ): 39 - 44 .
RUAN H J , ZHANG Q L , LIU F , et al . Physical simulation experiment on CO 2 storage mechanism in porous media [J ] . Journal of Liaoning Petrochemical University , 2024 , 44 ( 2 ): 36 - 41 .
范琳 , 杨磊 , 车晓甄 , 等 . CO 2 电化学还原制CO金属催化剂的研究进展 [J ] . 石油化工高等学校学报 , 2022 , 35 ( 6 ): 48 - 58 .
FAN L , YANG L , CHE X Z , et al . Research progress of metal catalysts for electrochemical reduction of CO 2 to CO [J ] . Journal of Petrochemical Universities , 2022 , 35 ( 6 ): 48 - 58 .
张天娇 . 一种高含CO 2 的天然气的脱碳系统及脱碳方法 : 202310151524.X [P ] . 2023-04-21 .
ZHANG T J . A decarbonization system and decarbonization method for natural gas with high CO 2 content : 202310151524.X [P ] . 2023-04-21 .
RUFFORD T E , SMART S , WATSON G C Y , et al . The removal of CO 2 and N 2 from natural gas: A review of conventional and emerging process technologies [J ] . Journal of Petroleum Science and Engineering , 2012 , 94/95 : 123 - 154 .
Shell Catalysts & Technologies . Switching to ADIP-X or Sulfinol-X [EB/OL ] . [ 2025-03-18 ] . https://catalysts. shell.com/switching-adip-x-sulfinol-x https://catalysts.shell.com/switching-adip-x-sulfinol-x .
周声结 , 贺莹 . 国内大规模MDEA脱碳技术在中海油成功应用: 以中海油东方天然气处理厂为例 [J ] . 天然气工业 , 2012 , 32 ( 8 ): 35 - 38+128 .
ZHOU S J , HE Y . Application of MDEA decarbonizing technology in CNOOC offshore gas fields: A case history of the CNOOC Dongfang Natural Gas Processing Plant [J ] . Natural Gas Industry , 2012 , 32 ( 8 ): 35 - 38+128 .
0
浏览量
0
下载量
0
CNKI被引量
关联资源
相关文章
相关作者
相关机构
 蜀公网安备51012202001533
 蜀公网安备51012202001533