石油与天然气化工
石油與天然氣化工
석유여천연기화공
CHEMICAL ENGINEERING OF OIL AND GAS
2014年
1期
17-23
,共7页
黄思宇%吴印强%朱聪%孙立鹏
黃思宇%吳印彊%硃聰%孫立鵬
황사우%오인강%주총%손립붕
凝液回收%DHX工艺%液化气铜片腐蚀%设备冻堵%丙烷收率%运行优化
凝液迴收%DHX工藝%液化氣銅片腐蝕%設備凍堵%丙烷收率%運行優化
응액회수%DHX공예%액화기동편부식%설비동도%병완수솔%운행우화
NGL recovery%DHX process%copper corrosion test in LPG%equipment freezing%propane recovery rate%operation optimization
高尚堡天然气处理装置采用丙烷+膨胀机制冷的D HX冷凝分离工艺回收C+3轻烃,由于原料气流量降低、气质组成中CO2和H2 S含量升高、处理装置操作参数变化造成液化气铜片腐蚀不合格、设备冻堵、丙烷收率低等问题。对装置存在问题进行分析后,改进处理工艺,脱除原料气中的CO2和H2 S至合理范围,解决液化气铜片腐蚀不合格和设备冻堵问题,降低酸性组分对装置冷凝温度的限制。筛选出影响装置丙烷收率和能耗的主要可调参数:膨胀机出口压力、脱乙烷塔操作压力、脱乙烷塔底温度、脱丁烷塔操作压力。通过HYSYS软件模拟结果分析装置主要可调参数对丙烷收率和装置能耗的影响规律,优化运行参数,实现丙烷收率和能耗之间的平衡,达到效益最大化。优化后,装置每年能耗费用增加108.1万元,但产品收入增加439.8万元,每年增加经济效益331.7万元。
高尚堡天然氣處理裝置採用丙烷+膨脹機製冷的D HX冷凝分離工藝迴收C+3輕烴,由于原料氣流量降低、氣質組成中CO2和H2 S含量升高、處理裝置操作參數變化造成液化氣銅片腐蝕不閤格、設備凍堵、丙烷收率低等問題。對裝置存在問題進行分析後,改進處理工藝,脫除原料氣中的CO2和H2 S至閤理範圍,解決液化氣銅片腐蝕不閤格和設備凍堵問題,降低痠性組分對裝置冷凝溫度的限製。篩選齣影響裝置丙烷收率和能耗的主要可調參數:膨脹機齣口壓力、脫乙烷塔操作壓力、脫乙烷塔底溫度、脫丁烷塔操作壓力。通過HYSYS軟件模擬結果分析裝置主要可調參數對丙烷收率和裝置能耗的影響規律,優化運行參數,實現丙烷收率和能耗之間的平衡,達到效益最大化。優化後,裝置每年能耗費用增加108.1萬元,但產品收入增加439.8萬元,每年增加經濟效益331.7萬元。
고상보천연기처리장치채용병완+팽창궤제랭적D HX냉응분리공예회수C+3경경,유우원료기류량강저、기질조성중CO2화H2 S함량승고、처리장치조작삼수변화조성액화기동편부식불합격、설비동도、병완수솔저등문제。대장치존재문제진행분석후,개진처리공예,탈제원료기중적CO2화H2 S지합리범위,해결액화기동편부식불합격화설비동도문제,강저산성조분대장치냉응온도적한제。사선출영향장치병완수솔화능모적주요가조삼수:팽창궤출구압력、탈을완탑조작압력、탈을완탑저온도、탈정완탑조작압력。통과HYSYS연건모의결과분석장치주요가조삼수대병완수솔화장치능모적영향규률,우화운행삼수,실현병완수솔화능모지간적평형,체도효익최대화。우화후,장치매년능모비용증가108.1만원,단산품수입증가439.8만원,매년증가경제효익331.7만원。
The DHX condensation and separation process by propane and expansion refrigera-tion are used to recovery C +3 in Gaoshangpu natural gas processing device .Due to the decreasing of feed gas flow rate ,the increasing of CO2 and H2 S content in feed gas ,and the variations of processing device operating parameters ,a series of problems occurred including copper corrosion test unqualified in LPG ,equipment freezing and low propane recovery rate .Based on the analysis of existing problems ,processing technology was improved and the CO 2 and H2 S of feed gas were removed to reasonable range to solve the problem of equipment corrosion ,freezing and reduce the limit of acid component to the condensing temperature .The main adjustable parameters which can influence propane recovery rate and energy consumption of the device were screened out ,in-cluding the expander outlet pressure ,deethanizer operating pressure ,deethanizer bottom temper-ature ,and debutanizer operating pressure .By using HYSYS simulation to analyze the influence of the main adjustable parameters on propane recovery rate and energy consumption and to opti-mize the operating parameters ,the balance between propane recovery and energy consumption was realized and maximum benefit was achieved .After optimization ,although the energy cost in-crease 1 .081 million yuan every year ,but the product income increase 4 .398 million yuan ,the annual economic benefit increase 3 .317 million yuan .