化工进展
化工進展
화공진전
CHEMICAL INDUSTRY AND ENGINEERING PROGRESS
2014年
8期
2219-2223
,共5页
龙文宇%李晓鸥%李东胜%刘宝柱%石岩
龍文宇%李曉鷗%李東勝%劉寶柱%石巖
룡문우%리효구%리동성%류보주%석암
溶剂萃取%石油%塔器%润滑油基础油%酸值
溶劑萃取%石油%塔器%潤滑油基礎油%痠值
용제췌취%석유%탑기%윤활유기출유%산치
solvent extraction%petroleum%column%lubricating base oil%acid value
用大庆尼罗混合减三线脱蜡油为原料,先后进行了工业装置理论塔板数标定、多级静态及中试规模的糠醛溶剂精制实验研究。结果表明,工业装置理论塔板数为2~3块。剂油体积比为6∶1的假二段实验与剂油体积比为3.2∶1的假四段实验精制油酸值均小于0.03mgKOH/g,收率分别为64.53%与75.33%。具有4块理论板数的中试装置在剂油体积比为2.81∶1条件下得到的精制油酸值为0.0246mgKOH/g,收率为78.01%。精制油产品质量能够满足HVI400SN润滑油基础油的质量要求。
用大慶尼囉混閤減三線脫蠟油為原料,先後進行瞭工業裝置理論塔闆數標定、多級靜態及中試規模的糠醛溶劑精製實驗研究。結果錶明,工業裝置理論塔闆數為2~3塊。劑油體積比為6∶1的假二段實驗與劑油體積比為3.2∶1的假四段實驗精製油痠值均小于0.03mgKOH/g,收率分彆為64.53%與75.33%。具有4塊理論闆數的中試裝置在劑油體積比為2.81∶1條件下得到的精製油痠值為0.0246mgKOH/g,收率為78.01%。精製油產品質量能夠滿足HVI400SN潤滑油基礎油的質量要求。
용대경니라혼합감삼선탈사유위원료,선후진행료공업장치이론탑판수표정、다급정태급중시규모적강철용제정제실험연구。결과표명,공업장치이론탑판수위2~3괴。제유체적비위6∶1적가이단실험여제유체적비위3.2∶1적가사단실험정제유산치균소우0.03mgKOH/g,수솔분별위64.53%여75.33%。구유4괴이론판수적중시장치재제유체적비위2.81∶1조건하득도적정제유산치위0.0246mgKOH/g,수솔위78.01%。정제유산품질량능구만족HVI400SN윤활유기출유적질량요구。
Furfural refining towards the third vacuum dewaxed distillate refined from the mixe d oil of Daqing and Nile was investigated. Calibration of theoretical plates number in the extraction column, multi-stage static extraction and pilot plant experiment were carried out. The results show that theoretical plates number in the column is 2 to 3. Under simulate-two-stage extractions,acid value of refined oil is below 0.03mgKOH/g when the value of volume ratio of solvent to oil (S/O) is 6. The acid value of refined oil meets the standard under simulate-four-stage extractions when the S/O is 3.2. The yields of refined oil are 64.53% and 75.33% respectively. Besides,acid value of the refined oil is 0.0246mgKOH/g in the pilot plant with four theoretical plates when the S/O is 2.81,and the yield of refined oil is 78.01%. The lubricating base oil meets the quality specification of HVI400SN.