β-萘甲醚合成新工藝
- 期刊名字:現(xiàn)代化工
- 文件大?。?10kb
- 論文作者:位青聰,葉文濤,宋輝,呂雯雯,趙敏,吳范宏
- 作者單位:華東理工大學(xué)化學(xué)與分子工程學(xué)院
- 更新時(shí)間:2020-10-22
- 下載次數(shù):次
第32卷第6期現(xiàn)代化工June 20122012年6月Modern Chemical industry·47β-荼甲醚合成新工藝位青聰,葉文濤,宋輝,呂雯雯,趙敏,吳范宏(華東理工大學(xué)化學(xué)與分子工程學(xué)院,上海200237)摘要:對(duì)B-萘甲醚的現(xiàn)有合成工藝進(jìn)行改進(jìn)。結(jié)合工業(yè)生產(chǎn),得到一條新的工藝,即采用一水合硫酸氫鈉作為催化劑B荼酚和甲醇于130~140℃下回流反應(yīng)14h。反應(yīng)收率最高達(dá)954%,與現(xiàn)有工藝相當(dāng),且隨著B(niǎo)-萘酚投量的增加,收率趨于穩(wěn)定(910%)。該工藝避免了現(xiàn)有工藝中的催化劑濃硫酸對(duì)設(shè)備的嚴(yán)重腐蝕和環(huán)境污染,可以應(yīng)用于工業(yè)化生產(chǎn)。關(guān)鍵詞-茶甲醚;合成;新工藝中圖分類(lèi)號(hào):0625322;TQ031.2文獻(xiàn)標(biāo)識(shí)碼:A文章編號(hào):0253-4320(2012)06-0047-02New synthesis process of B-naphthyl methyl etherWEI Qing-cong, YE Wen-tao, SONG Hui. Lv Wen-wen, ZHAO Min. WU Fan-hong. pSchooi of Chemistry and Molecular Engineering, East China University of Science and TechnologyShanghai 200237, China)Abstract: The existing synthetic process of B-naphthyl methyl ether is improved in this study Based on literaturesndustrial production, a new synthetic process is obtained, that is, B-naphthol reacts with methanol under refluxbetween 130-140C for 14 hours with sodium bisulfate monohydrate as the catalyst. The highest yield is 95.4%. Thestable yield(91. 0%)tends to be achieved with increasing the amount of B-naphthol. The new process avoids somedrawbacks in the existing route such as severe corrosion and environmental pollution caused by concentrated sulfuricid It makes the new process have great potential to be applied in industrial productionKey words: B-naphthyl methyl ether; synthesis; new processβ-萘甲醚又名橙花醚,具有橙花香味。作為口燒瓶中,加分水器冷凝管恒壓滴液漏斗,在磁力種合成香料,常用于食用香精和香皂中,也是合成萘攪拌下升溫至回流,然后一邊滴加甲醇,一邊將甲醇普生炔諾孕酮和米非可酮等藥物的中間體。工業(yè)蒸出,使得反應(yīng)體系的溫度相對(duì)穩(wěn)定。反應(yīng)數(shù)小時(shí),上常釆用濃硫酸催化β-萘酚與甲醇反應(yīng)或硫酸二然后冷卻,加入30mL乙酸乙酯和30m水,攪拌至甲酯與甲醇反應(yīng)來(lái)制備,但是這2種方法的收率不固體全溶,分液,有機(jī)相用質(zhì)量分?jǐn)?shù)為5%的氫氧化高,由于濃硫酸的腐蝕性和強(qiáng)氧化性,容易造成設(shè)備鈉水溶液洗滌,分液,有機(jī)相再用水洗后用無(wú)水硫酸的腐蝕,產(chǎn)生氧化偶聯(lián)的副產(chǎn)物,且硫酸二甲酯具有鈉干燥,得粗品,用無(wú)水乙醇重結(jié)晶后得白色鱗片狀劇毒性,因此開(kāi)發(fā)新的B-萘甲醚的合成方法對(duì)于節(jié)固體,熔點(diǎn)為72-~73℃;水相合并后用稀鹽酸酸化約成本和環(huán)保都具有積極的意義2。筆者以一水回收β-茶酚。合硫酸氫鈉作為催化劑,甲醇和B-茶酚為原料,對(duì)工藝進(jìn)行了改進(jìn)。2結(jié)果與討論實(shí)驗(yàn)2.1加料方式對(duì)反應(yīng)收率的影響1.1實(shí)驗(yàn)藥品及儀器實(shí)驗(yàn)中,B-茶酚和一水合硫酸氫鈉的摩爾比參β-萘酚、甲醇、硫酸氫鈉、無(wú)水硫酸鈉、氫氧化考文獻(xiàn)[3]中的比例。在實(shí)驗(yàn)中發(fā)現(xiàn),甲醇的用量鈉、濃鹽酸(以上藥品均為分析純)及乙酸乙酯(化對(duì)回流反應(yīng)的溫度有影響,亦對(duì)反應(yīng)的收率有影響。學(xué)純)。當(dāng)采用傳統(tǒng)回流方式——即在反應(yīng)瓶上裝回流冷凝WRS-1B型熔點(diǎn)儀, Brucker am400(400MHz)管的方式,由于甲醇的沸點(diǎn)較低(64.8℃),反應(yīng)體核磁共振儀。系不能夠升到較高的溫度(100℃以上),因此,為了1.2β萘甲醚的合成繼續(xù)提高反應(yīng)體系的溫度,采用了不同的加料方式,將14.4g(0.100mol)B-萘酚、5.0g(0.0362即對(duì)甲醇邊蒸出邊滴加的方式,通過(guò)控制滴加的速mol)→水合硫酸氫鈉和一定量甲醇放入100mL三率來(lái)間接調(diào)整反應(yīng)體系的溫度。收稿日期:2012-01-10作者簡(jiǎn)介:位青聰(1985-),男,碩上生, hanxia016@ o sina. corn;趙敏(1965-),男,副教授,研究方向?yàn)橛袡C(jī)合成和藥物合成,021-64253530,haomin6502@sina.com;吳范宏(1968-),男,博土,教授,研究方向?yàn)橛袡C(jī)氟化學(xué)及藥物和中間體合成,通訊聯(lián)系人,wh@eust現(xiàn)代化工第32卷第6期22反應(yīng)溫度對(duì)收率的影響2.5產(chǎn)品結(jié)構(gòu)的表征以0.0250mlB-萘酚投料質(zhì)量為基準(zhǔn),在不同實(shí)驗(yàn)合成所得的β-萘甲醚粗品用無(wú)水乙醇重的溫度范圍內(nèi)反應(yīng)6h,B-萘甲髒的收率見(jiàn)表1。結(jié)晶后得到白色鱗片狀固體,熔點(diǎn)為72~73℃,與表1溫度對(duì)收率的影響文獻(xiàn)值相符4;產(chǎn)品結(jié)構(gòu)經(jīng)H-NMR和紅外光譜確溫度/℃70~8090~100110~120130~140150~160認(rèn):H-NMR(400MHz,CDCl13),8:3.93(s,3H,收率/%60.565.471.575.374.5CH3),7.14(m,2H,ArH),7.34(m,1H,ArH),7. 44(m, IH, ArH), 7. 76(m, 3H, ArH ) IR( KBr),vr從表1可以看出,當(dāng)反應(yīng)溫度在130~140℃時(shí)cm:3055.0、300.6(ArH);2961.0、294.9收率較高,且溫度繼續(xù)增加后收率相對(duì)穩(wěn)定,故選擇288282835.5(C—H);1629.4、1596.1、15058此溫度進(jìn)行后續(xù)實(shí)驗(yàn)。1472.8(Ar);1259.6、1216.8、1029.1(C-0)。2.3反應(yīng)時(shí)間對(duì)收率的影響3結(jié)論以0.0250moB-萘酚投料質(zhì)量為基準(zhǔn),在130140℃下反應(yīng),反應(yīng)時(shí)間對(duì)收率的影響見(jiàn)表2。以n(B-萘酚):n(一水合硫酸氡鈉)=1:0.29表2反應(yīng)時(shí)間對(duì)收率的影響比例進(jìn)行投料反應(yīng),對(duì)甲醇采用邊滴加邊蒸出的加時(shí)間/h61214料方式,控制反應(yīng)溫度在130~140℃,反應(yīng)14h,收收率%75.380.688.791.294.893.5率最高達(dá)95.4%。產(chǎn)物收率隨著β-萘酚的投料質(zhì)量的增加趨于穩(wěn)定(91.0%)。該工藝在工業(yè)生產(chǎn)上操作可行,且一水合硫酸氫鈉價(jià)廉易得,對(duì)設(shè)備腐從表2可以看出,當(dāng)反應(yīng)溫度為14h時(shí),收率蝕小,可以取代濃硫酸應(yīng)用于工業(yè)化生產(chǎn)。最高,故選擇反應(yīng)時(shí)間為14ho2.4B-酚投料質(zhì)量對(duì)收率的影響參考文獻(xiàn)β-萘酚投料質(zhì)量對(duì)收率的影響見(jiàn)表3「1]吳飛陳天云4A分子篩在合成2-萘甲醚中的應(yīng)用[J].化學(xué)反表3B酚投料質(zhì)量對(duì)收率的影響應(yīng)工程與工藝,2002,18(2):149-152投料質(zhì)量/g3.67.214.421.628.857.6[2]曾慶欂.β-萘甲醚的相轉(zhuǎn)移催化合成[J].中國(guó)醫(yī)藥工業(yè)雜志,收率/%94.895.095.491.291.191.01997,28(4):187[3]俞善信,管仕斌倇酸氪鈉催化合成β-萘甲醚[J].湘南學(xué)院學(xué)報(bào),2004,25(5):從表3可以看出,隨著β-萘酚投料質(zhì)量的增[4]俞善信,俞超源氯化鐵催化合成β-萘甲醚[J].現(xiàn)代化工,加,產(chǎn)物的收率趨于穩(wěn)定。199,(7):29-30.■凸4444畫(huà)小▲心卓心4心學(xué)(上接第46頁(yè))[ 22] Pinto M FC, Noronha F B, Borges L E P. Proceedings of the 17th[17 Kim K Boo S I, Ahn H G. Preparation and characterization of thenorth american catalysis society meeting[ C]. Toronto, Canadabimetallic Pt-Au/ZnO/AL,O3 catalysts Influence of Pt-Au molar2001:295ratio on the catalytic activity for toluene oxidation[ J]. Journal of[23 Narui K, Yata H. Effects of addition of Pt to PdO/Al, O, catalyst onIndustrial and Engineering Chemistry, 2009, 15(1): 92-97catalytic activity for methane combustion and TEM observations of[18 Shim W G, Lee j W, Kim S C. Analysis of catalytic oxidation ofsupported particles[J]. Applied Catalysis A: General, 1999, 179aromatic hydrocarbons over supported palladium catalyst with dif-(1/2):165-17[25] Kim H S, Kim T W, H Koh L, et al. Complete benzene oxidation o-ferent pretreatments based on heterogeneous adsorption propertiesver Pt-Pd bimetal catalyst supported on y-alumina: Influence of Pt[J. Applied Catalysis B: Environmental, 2008, 84(1/2): 133-141Pd ratio on the catalytic activity[ J]. Applied Catalysis A: General[ 19] Huang S, Zhang C, He H. Complete oxidation of o-xylene over Pd2005,280(2):125-13AL,O3 catalyst at low temperature[J]. Catalysis Today, 2008, 13926] Kim SC, Nahm S W, Shim WG, et al. Influence of physicochemical(1/2):l5-23treatments on spent palladium based catalyst for catalytic oxidation120 Dege P, Pinard L, Magnoux P, et aL. Catalytic oxidation of volatileof VOCs[ J] Journal of Hazardous Materials, 2007, 141(1): 305organic compounds I. Influence of the physicochemical character314istics of Pd/HFAU catalysts on the oxidation of o-xylene[J]. A[27] Kim H S, Kang M, Song M W, et al. XPS analysis of the effect of Ptplied Catalysis B: Environmental, 2000, 27(1): 17-26addition to pd catalysts for complete benzene oxidation[ J].Reac[21] Su S C, Carstens J N, Bell A T. A Study of the synamics of Pd oxition Kinetics and Catalysis Letters, 2004, 81(2): 251-257.dation and PdO reduction by H2 and CH4[J] Journal of Catalysis28]土麗敏,儲(chǔ)偉陳慕華,等揮發(fā)性有機(jī)化合物催化燃燒用鉑基1998,176(1):125催化劑的研究進(jìn)展[J現(xiàn)代化工,2006,26(5):24-28
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