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1.
以自制白果粉为原料,分析了提取溶剂、粉料粒度、提取温度、超声波功率、料液比、提取时间及提取次数对白果出油率的影响。结果表明:石油醚(沸程60~90℃)是较适宜的提取溶剂,出油率为3.88%。最佳提取工艺为:白果粉粉碎度80目,提取温度25℃,超声波提取功率200 W,料液比1∶25(g/ml),每次提取时间40 min,提取次数2次。最优工艺条件下,出油率为3.86%,较索氏提取法,该工艺对白果粗脂肪的提取率为98.71%。  相似文献   

2.
对喷动循环流化床落叶松树皮快速热解过程中反应温度、物料粒径、进料速率及气体流量对热解产物产率的影响以及这4个因素共同作用对生物油产率的影响进行研究.结果表明:反应温度是影响热解产物产率的主要因素,气体流量影响较显著,在试验范围内物料粒径、进料速率影响不显著;喷动循环流化床最佳制备液体产物--生物油快速热解工艺条件为:反应温度550℃,物料粒径0.2~0.3 mm,进料速率20 r·min-1,气体流量25m3·h-1.  相似文献   

3.
开发了一种应用超临界二氧化碳技术从烟草提取物中同时分离茄尼醇和辅酶Q10的方法。研究了萃取时间、压力、温度和二氧化碳流量对茄尼醇和辅酶Q10收率的影响。结果表明,最优的提取条件为:萃取时间60 min,萃取压力36 MPa,萃取温度59℃,二氧化碳流量10 kg/h。在优化的超临界二氧化碳提取条件下,茄尼醇和辅酶Q10的提取率分别为1.84%和2.07 mg/g,茄尼醇和辅酶Q10在超临界二氧化碳萃取物中的含量分别为52.3%和3.6%。  相似文献   

4.
在实验条件下,考察反应温度、升温速率、物料颗粒大小等因素对蔗渣在水蒸气中的热解气化特性的影响。实验结果表明,热解终温越高,物料粒径越小,越有利于产生高质量的热解气。在先到达热解终温,再通入水蒸气的操作条件下,升温速率的改变对气化效果的影响并不突出,而热解终温是热解气化过程主要的决定因素。实验在最佳条件,温度采用粉末物料在1 000℃进行热解可以得到高热值合成气10 M J/Nm3,和较高的产气率1.7 m3/kg。  相似文献   

5.
棕榈壳热解失重特性及动力学研究   总被引:1,自引:0,他引:1  
采用热重-红外联用(TG-FTIR)、裂解-气相色谱/质谱联用(Py-GC/MS)技术和小型固定床装置,考察了棕榈壳的热解失重过程和产物特性,并进一步评价了热解半焦的气化反应性。结果表明:棕榈壳热解失重过程大致分为干燥(25~236℃,3.42%)、主失重(236~400℃,52.31%)和炭化(400~850℃,14.90%)3个阶段,1.5级或2级反应可以较好描述棕榈壳热解反应的主失重过程;升温速率10~30 K/min下,反应表观活化能为67.63~76.47 k J/mol;热解过程主要气体产物的释放量顺序分别为CO2、H2O、CH4和CO;600~850℃下,棕榈壳主要热解产物为液相产物,其质量产率36.8%~50.9%,能量产率41.3%~58.9%,主要组分包括苯酚、乙酸、十八烷酸、十六烷酸、4-烯丙基-2,6-二甲氧基苯酚等物质,其中苯酚GC含量较高(12.56%~15.49%),这可能主要与原料木质素的含量较高有关;固相产物的质量和能量产率分别为20.6%~26.7%和27.4%~35.0%,其CO2气化反应性相对低于稻秆、木粉等常见生物质。  相似文献   

6.
The extraction of phenolic compounds from eucalyptus (Eucalyptus globulus) bark was examined with the aim of analyzing the potential of the extracts as natural antioxidants. Experiments were planned according to a 23 factorial design to analyze the influence of temperature and Na2SO3 and NaOH concentrations in aqueous solutions on extraction yield, extract total phenols content, ferric reducing antioxidant power (FRAP), and number- and weight-average molecular weights. Extract total phenols content and FRAP antioxidant activity in the ranges 0.91–2.58?g gallic acid equivalent (GAE)/100?g oven-dried bark and 4.70–11.96?mmol ascorbic acid equivalent (AAE)/100?g oven-dried bark, respectively, demonstrated the potential of eucalyptus bark as a source of antioxidant compounds. Extraction at the highest temperature (100°C), the lowest Na2SO3 concentration (1.5% on oven-dried bark), and without NaOH provided the highest extract total phenols content and FRAP antioxidant activity. Those eucalyptus bark extracts with lower molecular weight showed higher antioxidant activity. Matrix-assisted laser desorption ionization time-of-flight and reverse-phase high-performance liquid chromatography electrospray ionization time-of-flight mass spectrometry revealed the presence of polygalloyl glucoses, catechin, epicatechin, ellagic acid, quercetin-3-o-rhamnoside, and isorhamnetin in eucalyptus bark aqueous extracts.  相似文献   

7.
崔连喜 《绿色科技》2014,(2):156-158
采用聚丙烯中空纤维膜接触器,用一乙醇胺(M EA )、二乙醇胺(DEA )和氨基乙酸钾(PG )作为吸收剂对烟气中的CO2进行了吸收实验,研究气体流速、吸收剂流速和浓度等因素对CO2脱除率和传质速率的影响。结果表明:以上吸收剂分离吸收CO2的效率由大到小依次是PG、M EA、DEA。CO2的脱除率和传质速率随吸收剂浓度和流速的提高均增加;CO2脱除率随气体流量的增加而减小,但传质速率却随之增加。  相似文献   

8.
Summary We present experimental data on hydrolysis of wood in high temperature short residence time (HTST) and low acid concentration conditions. Effects of temperature, acid concentration, particle size and liquid/solid ratio are discussed. A kinetic model is proposed which accounts for effects of temperature and acid concentration. This kinetic model is used to predict performance of a twin-screw extruder as a hydrolyser which consists of ideal mixed flow or plug flow reactor units in series.Symbols A Acid concentration in liquid phase - A Acid concentration in solid phase - A0 Initial mass of sulphuric acid, g - C Cellulose content of solid phase, % - d Diameter of wood particles, m - E1 Activation energy of cellulose hydrolysis, cal. mol-1 - E2 Activation energy of glucose degradation, cal. mol-1 - F Objective function, refers to Eq. (5) - G Glucose yield - Ge Glucose yield at equilibrium - Gi, exp Experimental glucose yield (Eq. (5)) - Gi, th Calculated glucose yield (Eq. (5)) - Gmax Maximum glucose yield - k* Parameter defined by Eq. (9) - k1 Rate constant of cellulose hydrolysis, s-1 - k2 Rate constant of glucose degradation, s-1 - k 1 * Apparent rate constant of cellulose hydrolysis, s-1 - k 2 * Apparent rate constant of glucose degradation, s-1 - k10 Pre-exponential factor of constant k1, s-1 - k20 Pre-exponential factor of constant k2, s-1 - K Parameter defined in Table 3 - m Constant - mg Mass of glucose produced, g - M0 Initial mass of wood, g - M Mass of saturated steam delivered, g - M Mass of saturated steam delivered after 120 s of reaction time, g - m0 Initial mass of water, g - n Constant - N Number of reactor units - qi Volume flow rate in reactor units, m3 · s-1 - rg Conversion rate of glucose, s-1 - R Ideal gas constant, 1.987 cal · mol-1 K-1 - t Reaction time, s - T Temperature, K - Vi Volume of reactor units, m3 - W Water content of wood sample, % - X, X Parameters defined in Table 3 - Y, Z Parameters defined in Table 3 - Constant defined in Eq. (4), s-1 - v Number of experimental points (Eq. (5)) - i Residence time in plug flow unit, s - i Residence time in mixed flow unit, s  相似文献   

9.
研究超临界CO2萃取(SCDE)鸦胆子油的动力学.建立了超临界CO2萃取鸦胆子油的质量守恒微分方程动力学模型,对萃取过程进行模拟.该模型直观地模拟出了萃取过程中萃取床内CO2流体中溶质质量分数在萃取时间和萃取床高度上的分布,并且模拟出了萃取釜出口处CO2流体中溶质质量分数随萃取时间的变化.该模型能较好地模拟实际萃取过程,模拟值与实验值之间的误差在10%以内,能较好地反映萃取压力和萃取温度等工艺参数对萃取收率和萃取过程的影响.  相似文献   

10.
白桦树皮中桦木醇超临界二氧化碳萃取的研究(英文)   总被引:4,自引:0,他引:4  
桦木醇,一种药用五环三萜成分,大量存在于白桦(Betulaplatyphlly)树皮中。白桦树皮于2000年9月采集自黑龙江省塔源林场。超临界流体萃取技术(SFE)是一种新型分离技术,广泛用于药物和天然产物生产。本文研究了利用超临界CO2萃取技术从白桦皮中提取桦木醇的工艺条件,系统分析了携带剂用量、萃取压力和萃取温度等参数对桦木醇提取率的影响。结果表明,最佳的萃取条件为:每克桦树皮粉所用携带剂用量为1.5mL,萃取压力为20Mpa,萃取温度为55C,CO2流量为10kg/h,分离压力和分离温度分别为5.5Mpa和50C。图4参6。  相似文献   

11.
云南松花粉超临界CO2脱脂研究   总被引:3,自引:0,他引:3  
应用超临界CO2 萃取技术研究云南松花粉脱脂的工艺。依据影响脂肪提取率的温度、压力、时间及流量 ,采用 4因素 3水平的正交实验设计进行实验 ,得到云南松花粉脱脂的可靠工艺参观数为 :温度T2 ,压力P3 ,时间H2 ,流量L2 ,进而分别对参试的 4因素与云南松花粉脱脂率的关系作了分析。  相似文献   

12.
超声法提取薏苡仁油的工艺研究   总被引:1,自引:0,他引:1  
采用超声波法提取薏苡仁油,对其中的影响因素提取溶剂、药材粒径、提取时间、提取温度、料液比等进行系统研究。结果表明:将薏苡仁药材粉碎至粒径60目,按料液比1∶3.5加入无水乙醇为提取溶剂,在60℃温度下提取40 min ,所得提取率最高为11.8%。该提取工艺具有提取时间短,效率高,节省溶剂的特点。  相似文献   

13.
采用喷动循环流化床快速热解系统对落叶松树皮进行快速热解制备高酚类物质含量生物油,考察反应温度、粒径、进料速率和气体流量对生物油中酚类物质含量的影响,以生物油中酚类物质含量为目标,优化快速热解工艺.结果表明:反应温度、粒径是影响生物油中酚类物质含量的关键因素;制备高酚类物质含量生物油的喷动循环流化床快速热解最佳工艺为:反应温度823K,粒径0.3~ 0.45mm,进料速率50 r/min,气流量15 m3/h.  相似文献   

14.
超声波法提取木材中的阿拉伯半乳聚糖的研究   总被引:1,自引:5,他引:1  
应用超声波技术浸提兴安落叶松(Larix gmelinii Rupr.)木材加工剩余物中的阿拉伯半乳聚糖。研究了影响阿拉伯半乳聚糖得率的提取条件,包括超声波功率、料液比、原料粒度和浸提时间。将超声波提取与传统提取和微波提取进行比较,并利用红外光谱和紫外吸收光谱分析浸提物。超声波法提取的粗产品在280nm处的紫外吸光度最小;产品质量最接近标准品。在单因素试验中超声波提取的粗阿拉伯半乳聚糖最高提取率为16.61%,比传统浸提法高。  相似文献   

15.
超临界C02萃取沙棘果渣中β--胡萝卜素的初步研究   总被引:2,自引:0,他引:2  
用超临界CO2流体萃取沙棘果渣得到橘红色提取物,经试验确定了超临界CO2流体萃取沙棘果渣的最佳工艺条件。讨论了萃取压力,萃取温度,分离压力,分离温度,CO2流量,时间等对沙棘果渣有效成分提取的影响,并对沙棘果渣提取物性质做了初步试验。  相似文献   

16.
我国农业害螨的抗药性越发严重,在防治过程中害螨的天敌也受到杀伤,造成害螨的再猖獗,严重影响农作物及经济林的产量和品质(Kalaisekar et al.,2003;Shi et al.,2004)。瑞香狼毒(Stellera chamaejasme)是对我国草地危害较重的有毒植物之  相似文献   

17.
超临界CO_2流体萃取辣木籽油工艺研究初报   总被引:3,自引:3,他引:0  
初步研究了SFE-CO2辣木籽油工艺,探索了萃取压力、萃取温度、萃取时间和萃取CO2流量等主要因素对萃取率的影响,并通过正交试验进行了工艺参数筛选。结果表明:当萃取压力30MPa,温度50℃,时间3h,CO2流量23L/h,SFE-CO2辣木籽油效果最佳,且SFE-CO2辣木籽油工艺流程简单,无溶媒残留,品质好,纯度高,外观清亮,过氧化值0.431meq/kg。  相似文献   

18.
研究了超临界CO2流体萃取柑橘皮精油的工艺条件并对其化学成分进行了分析。考察了在超临界CO2条件下,萃取时间、萃取压力、萃取温度、CO2流量和分离温度等因素对精油得率的影响,并通过正交试验优化得到最佳工艺条件,用GC-MS法测定柑橘皮精油的化学组成。结果显示最佳工艺条件为:萃取温度40℃,萃取压力20 MPa,分离温度50℃,萃取时间60 min,CO2流量25 kg/h。在此条件下,精油得率为0.86%。GC-MS测定结果显示柑橘皮精油主要由5,5’-二甲氧基-3,3’-二甲基-2,2’-联二萘-1,1’,4,4’-四酮组成(35.54%),其次还含β-羟基-甲基炔诺酮-甲基肟(24.60%)。  相似文献   

19.
印楝作为植物源木材防腐剂活性物提取的重要来源深受研究人员的重视,对其活性物的萃取工艺也多种多样。本文采用了超声波震荡法、微波萃取法及水浴搅拌法对印楝种子粉末进行提取,在不同物液比(1∶8、1∶10、1∶12)、不同温度(30、40、50℃)下,对比分析三种工艺的粗提率。结果表明,三种提取工艺的提取率均随着温度的升高而增大,随着物液比(印楝种子粉末与乙醇-水之比)的降低而增大;在对印楝种子活性成分粗提取时的三种方法比较,温度控制在50℃,物液比为1∶12时,微波萃取法的提取率最高。  相似文献   

20.
Effects of temperature on growth and wood anatomy were studied in young European beech (Fagus sylvatica L.) grown in 7-l pots for 2.5 years in field-phytotron chambers supplied with an ambient (approximately 400 micromol mol-1) or elevated (approximately 700 micromol mol-1) carbon dioxide concentration ([CO2]). Temperatures in the chambers ranged in increments of 2 degrees C from -4 degrees C to +4 degrees C relative to the long-term mean monthly (day and night) air temperature in Berlin-Dahlem. Soil was not fertilized and soil water and air humidity were kept constant. Data were evaluated by regression analysis. At final harvest, stem diameter was significantly greater at increased temperature (Delta1 degrees C: 2.4%), stems were taller (Delta1 degrees C: 8.5%) and stem mass tree-1 (Delta1 degrees C: 10.9%) and leaf area tree-1(Delta1 degrees C: 6.5%) were greater. Allocation pattern was slightly influenced by temperature: leaf mass ratio and leaf area ratio decreased with increasing temperature (Delta1 degrees C: 2.3% and 2.2% respectively), whereas stem mass/total mass increased (Delta1 degrees C: 2.1%). Elevated [CO2] enhanced height growth by 8.8% and decreased coarse root mass/total mass by 10.3% and root/shoot ratio by 11.7%. Additional carbon was mainly invested in aboveground growth. At final harvest a synergistic interaction between elevated [CO2] and temperature yielded trees that were 3.2% taller at -4 degrees C and 12.7% taller at +4 degrees C than trees in ambient [CO2]. After 2.5 seasons, cross-sectional area of the oldest stem part was approximately 32% greater in the +4 degrees C treatment than in the -4 degrees C treatment, and in the last year approximately 67% more leaf area/unit tree ring area was produced in the highest temperature regime compared with the lowest. Elevated [CO2] decreased mean vessel area of the 120 largest vessels per mm2 by 5.8%, causing a decrease in water conducting capacity. There was a positive interaction between temperature and elevated [CO2] for relative vessel area, which was approximately 38% higher at +4 degrees C than at -4 degrees C in elevated [CO2] compared with ambient [CO2]. Overall, temperature had a greater effect on growth than [CO2], but elevated [CO2] caused quantitative changes in wood anatomy.  相似文献   

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