石油与天然气化工
石油與天然氣化工
석유여천연기화공
CHEMICAL ENGINEERING OF OIL AND GAS
2015年
4期
19-23
,共5页
纤维膜%液化石油气%脱硫%脱硫醇%应用
纖維膜%液化石油氣%脫硫%脫硫醇%應用
섬유막%액화석유기%탈류%탈류순%응용
fiber film%liquefied petroleum gas(LPG)%desulfurization%mercaptan removal%appli-cation
介绍了纤维膜脱硫组合技术在某石化公司液化石油气脱硫脱硫醇装置上的工业应用情况。结果表明,纤维膜脱硫组合技术具有适用性强、开工过程简单等优点。脱硫脱硫醇后催化裂化装置液化石油气中总硫质量浓度降至16.3~16.8 mg/m3,铜片腐蚀等级为1a ,延迟焦化装置液化石油气中总硫质量浓度降至50.8~77.8 m g/m3,铜片腐蚀等级为1a ,均满足产品质量要求。经过水洗后,两装置循环碱性洗水中硫化物质量浓度分别为17.91 m g/L和73.83 m g/L ,回收大量副产物二硫化物;废碱液经过碱液再生后,碱液质量分数均大于15%,满足纤维膜脱硫醇的需要。碱渣经过湿法氧化处理后,满足排放标准。
介紹瞭纖維膜脫硫組閤技術在某石化公司液化石油氣脫硫脫硫醇裝置上的工業應用情況。結果錶明,纖維膜脫硫組閤技術具有適用性彊、開工過程簡單等優點。脫硫脫硫醇後催化裂化裝置液化石油氣中總硫質量濃度降至16.3~16.8 mg/m3,銅片腐蝕等級為1a ,延遲焦化裝置液化石油氣中總硫質量濃度降至50.8~77.8 m g/m3,銅片腐蝕等級為1a ,均滿足產品質量要求。經過水洗後,兩裝置循環堿性洗水中硫化物質量濃度分彆為17.91 m g/L和73.83 m g/L ,迴收大量副產物二硫化物;廢堿液經過堿液再生後,堿液質量分數均大于15%,滿足纖維膜脫硫醇的需要。堿渣經過濕法氧化處理後,滿足排放標準。
개소료섬유막탈류조합기술재모석화공사액화석유기탈류탈류순장치상적공업응용정황。결과표명,섬유막탈류조합기술구유괄용성강、개공과정간단등우점。탈류탈류순후최화열화장치액화석유기중총류질량농도강지16.3~16.8 mg/m3,동편부식등급위1a ,연지초화장치액화석유기중총류질량농도강지50.8~77.8 m g/m3,동편부식등급위1a ,균만족산품질량요구。경과수세후,량장치순배감성세수중류화물질량농도분별위17.91 m g/L화73.83 m g/L ,회수대량부산물이류화물;폐감액경과감액재생후,감액질량분수균대우15%,만족섬유막탈류순적수요。감사경과습법양화처리후,만족배방표준。
The industrial application of the fiber film desulfurization combination technology in liq‐uefied petroleum gas sweetening unit in a petrochemical company was introduced .The result indicated that the fiber film desulfurization combination technology had the advantages of great applicable activ‐ity and simple starting‐up .The total sulfur content in liquefied petroleum gas in fluid catalytic crack‐ing unit may reduce to 16 .3-16 .8 mg/m3 after sweetening ;and the corrosion grade of copper sheet was 1a .The total sulfur concentration of liquefied petroleum gas in delayed coking unit may reduce to 50 .8-77 .8 mg/m3 ,and the corrosion grade of copper sheet was 1a ,meeting the product quality re‐quirement .After water washing ,the sulfide concentrations in alkaline washing water of two sets of u‐nits were 17 .91 mg/L and 73 .83 mg/L ,respectively ,recovering the disulfides as by‐products .The mass fraction of regenerated lye was above 15% ,meeting the sweetening requirment of fiber film . The alkaline sludge could meet the discharge requirements after treated by wet oxidation .