化工进展
化工進展
화공진전
CHEMICAL INDUSTRY AND ENGINEERING PROGRESS
2014年
6期
1596-1600,1606
,共6页
孙佰仲%白林峰%王擎%张欣欣
孫佰仲%白林峰%王擎%張訢訢
손백중%백림봉%왕경%장흔흔
页岩油泥%热化学清洗%化学药剂%回收%环境%污染
頁巖油泥%熱化學清洗%化學藥劑%迴收%環境%汙染
혈암유니%열화학청세%화학약제%회수%배경%오염
oil shale sludge%thermo chemical washing%chemical reagent%recovery%environment%pollution
含油污泥主要产生于油田或炼油厂,对环境造成污染,部分油资源浪费。目前国内外局限于对石油油泥处理,但对页岩油泥处理少有报道,为了解决这一问题,本文提出用热化学法处理页岩油泥。本文以汪清炼油厂油泥为样品,采用热化学法清洗页岩油泥,回收页岩油,并获取最佳清洗工况参数。纯水清洗页岩油泥,考察温度、搅拌时间、搅拌频率、液固比对清洗效率的影响,并确定初始工况参数。通过化学药剂筛选、复配,确定AEO-9∶Na2SiO3=1∶2为最佳清洗剂配方。正交试验确定最佳清洗工况参数。试验分析表明,当清洗温度为75℃、液固比为8∶1、搅拌频率220r/min、搅拌时间30min、药剂投加量为4.0g/L时,含油率为45.26%样品油泥经热化学法清洗后,油泥残油率降为3.03%。清洗液可循环利用,分离出的页岩油经处理后可回收利用,将清洗后的油泥残渣与固硫剂、页岩粉尘等混合后压碇成型,经干燥,进行低温干馏生产,从而实现页岩油泥的资源化、无害化、减量化。
含油汙泥主要產生于油田或煉油廠,對環境造成汙染,部分油資源浪費。目前國內外跼限于對石油油泥處理,但對頁巖油泥處理少有報道,為瞭解決這一問題,本文提齣用熱化學法處理頁巖油泥。本文以汪清煉油廠油泥為樣品,採用熱化學法清洗頁巖油泥,迴收頁巖油,併穫取最佳清洗工況參數。純水清洗頁巖油泥,攷察溫度、攪拌時間、攪拌頻率、液固比對清洗效率的影響,併確定初始工況參數。通過化學藥劑篩選、複配,確定AEO-9∶Na2SiO3=1∶2為最佳清洗劑配方。正交試驗確定最佳清洗工況參數。試驗分析錶明,噹清洗溫度為75℃、液固比為8∶1、攪拌頻率220r/min、攪拌時間30min、藥劑投加量為4.0g/L時,含油率為45.26%樣品油泥經熱化學法清洗後,油泥殘油率降為3.03%。清洗液可循環利用,分離齣的頁巖油經處理後可迴收利用,將清洗後的油泥殘渣與固硫劑、頁巖粉塵等混閤後壓碇成型,經榦燥,進行低溫榦餾生產,從而實現頁巖油泥的資源化、無害化、減量化。
함유오니주요산생우유전혹련유엄,대배경조성오염,부분유자원낭비。목전국내외국한우대석유유니처리,단대혈암유니처리소유보도,위료해결저일문제,본문제출용열화학법처리혈암유니。본문이왕청련유엄유니위양품,채용열화학법청세혈암유니,회수혈암유,병획취최가청세공황삼수。순수청세혈암유니,고찰온도、교반시간、교반빈솔、액고비대청세효솔적영향,병학정초시공황삼수。통과화학약제사선、복배,학정AEO-9∶Na2SiO3=1∶2위최가청세제배방。정교시험학정최가청세공황삼수。시험분석표명,당청세온도위75℃、액고비위8∶1、교반빈솔220r/min、교반시간30min、약제투가량위4.0g/L시,함유솔위45.26%양품유니경열화학법청세후,유니잔유솔강위3.03%。청세액가순배이용,분리출적혈암유경처리후가회수이용,장청세후적유니잔사여고류제、혈암분진등혼합후압정성형,경간조,진행저온간류생산,종이실현혈암유니적자원화、무해화、감양화。
Oil sludge is mainly produced in the oil fields and refineries,causing environment pollution,and wasting some oil resources. Recent research on oil sludge cleaning was limited to oil sludge treatment,with little focus on oil shale sludge treatment. This paper presented thermo chemical method to treat oil shale sludge. Oil shale sludge from Wangqing Oil Refinery was used as the sample. Washing media for oil shale sludge treatment was pure water. The study investigated the influencing factors including temperature,agitate time,agitate rate,liquid-solid ratio on the washing efficiency, and the initial conditions were determined. After screening and remixing,AEO-9∶Na2SiO3=1∶2(the mass ratio)was regarded as the optimal ratio. Orthogonal experiments were conducted to determine optimal washing parameters. The results showed that residual oil rate was reduced to 3.03% from 45.26%in the sample after agitating for 30 min at 75℃ with agitation speed at 220 r/min,liquid-solid ratio at 8∶1,chemical reagent concentration at 4.0g/L. Chemical reagent solvents can be recycled,oil recovery can be used after treatment. After mixing,the residual oil sludge was treated with sulfur-fixing agent and shale dust,then the mixture was molded and dried. The final products can be sent to retort for low temperature retorting.