共查询到18条相似文献，搜索用时 140 毫秒
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该文通过4因素5水平二次正交旋转组合试验，研究了用于浸油的玉米胚挤压膨化预处理过程中的挤压系统参数(套筒温度、模孔孔径、物料含水率、螺杆转速)对考察指标(残油率、剪切强度、密度)的影响规律。得到最佳挤压工艺参数：模孔直径9 mm，物料出口温度93℃，喂入物料含水率13.3%，螺杆转速238 r/min，在此条件下得出残油率最优值为0.40%。和传统工艺相比，浸提时间缩短一半，膨化物的密度与轧坯和预轧样相比分别增加29.3%和13.8%。只要参数选择合适，可使原设备的浸出能力提高60%～120%。 相似文献
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菜籽挤压膨化系统参数对出油率影响的试验研究 总被引：7，自引：1，他引：7
该文研究了用于浸油的一种菜籽挤压膨化预处理工艺(油菜籽清理—带壳粉碎—膨化—浸油)的可行性，油菜籽挤压膨化系统参数(模孔孔径、套筒温度、物料含水率、螺杆转速)对各考察指标(粕的残油率、膨化物含油率及榨笼出油率)的影响规律，挤压膨化系统优化参数的范围为模孔孔径8～12 mm、套筒温度105～125℃、物料含水率6.6%、螺杆转速35～55 r/min。研究表明：只要参数选择合适，带壳油菜籽清理、粉碎、挤压膨化、浸出的菜籽浸油预处理工艺是可行的，且残油率较低。该菜籽挤压膨化浸油预处理工艺可供生产参考。 相似文献
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用于浸油的大豆挤压膨化研究 总被引：17，自引：5，他引：12
研究了大豆挤压膨化系统诸参数（模孔孔径、挤压温度、物料含水率、螺杆转速）对大豆粗脂肪、豆粕残油率、蛋白质含量、及其氮可溶解指数、脲酶活性的影响规律和挤压膨化系统最佳参数。结果表明,只要系统参数选择合适,可使膨化后大豆粗脂肪基本不减少,粕残油小于１％,使原设备浸出能力增加１５０％。且膨化前后大豆粗蛋白含量基本不变,氨基酸没有损失,膨化后氮可溶解指数和脲酶活性均略有下降。同时省去目前大豆膨化浸油和传统浸油过程的破碎、软化、轧胚、蒸炒等工序。需增加粉碎、膨化工序。 相似文献
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合理的原料预处理工艺可以提高玉米淀粉出酒率,该文用单螺杆挤压膨化机对脱胚玉米进行挤压膨化,以模孔直径、套筒温度、物料含水率、螺杆转速和酵母添加量作为因素,以挤压膨化脱胚玉米淀粉出酒率为考察指标,采用5因素5水平(1/2实施)进行二次正交旋转组合试验设计,探讨了挤压膨化工艺参数和酵母添加量对挤压膨化脱胚玉米淀粉出酒率的影响规律,得到了优化的工艺参数:模孔直径为12mm,套筒温度140℃,物料含水率19%,螺杆转速200r?min-1,在酵母添加量为0.4%时,玉米淀粉出酒率可以达到55.81%。 相似文献
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该文研制了一种新型水稻精量穴直播排种轮，用4种不同类型的稻种对5种不同型孔的排种轮进行了排种试验，结果表明：瓢形型孔充种性能优于其他型孔形式，粒数为2～6粒种子的穴数在90％以上，漏播率小于5%，穴距、穴径符合农艺要求，实现了精量播种。伤种率对比试验表明，瓢形型孔的排种轮对水稻发芽率无显著影响。该文还进行了不同的瓢形型孔个数的排种对比试验，确定了适合该排种轮的型孔个数。研究工作为水稻精量穴直播排种轮的设计提供了依据。 相似文献
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生物质制粒机环模的磨损机理分析 总被引：2，自引：2，他引：0
环模是制粒机的核心部件,目前存在磨损快、寿命短等问题。该文对X46Cr13钢环模进行600 h实际生产状态下的磨损试验;对环模内壁和模孔内壁的磨损量与表面硬度进行测量;对磨损面进行表观形貌和微观磨损形貌观察;从宏观和微观角度对磨损机理进行分析,旨在通过研究环模磨损机理与磨损分布规律,对环模改进提出建议。结果表明：不同磨损位置起主导作用的磨损机制有所不同;环模内壁磨损十分严重,磨损机理为以微切削作用为主的磨粒磨损和疲劳磨损交互作用;模孔内壁磨损量较小,模孔入口附近以磨粒磨损为主,出口附近则以疲劳磨损为主,从模孔入口到出口磨损量呈指数形式逐渐减小,磨损由磨粒磨损为主逐渐向疲劳磨损为主过渡。研究结果可为改善环模耐磨性能和延长使用寿命提供参考。 相似文献
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Efficiency of oil extraction from corn germ was improved by the extrusion pretreatment, and residual oil was taken as the index of this oil extraction process. An orthogonal rotation combination test design of five levels and four factors, consisting of the moisture of material, screw speed, barrel temperature, and die nozzle diameter, was employed to optimize the model and reaction condition. The optimum parameters of extrusion were as follows: moisture of material, W = 12%; extrusion temperature, T = 105°C; screw speed, n = 185 rpm; die nozzle diameter, Φ = 9 mm × 3. Under these optimum conditions, residual oil of this process was 0.61–0.66%, which was lower than residual oil by pressing alone (residual oil of 5–6%) or by a combination of prepressing and hexane extraction (residual oil of nearly 2%). The corn oil obtained by the optimum extrusion parameters was analyzed, and iodine value, acid value, peroxide value, and saponification value were 1,250 g/kg, 400 mg/kg, 5.1 mmol/kg, and 189%, respectively. 相似文献
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挤压膨化大米做啤酒辅料的试验研究 总被引：12，自引：4，他引：12
该文通过实验室试验,研究了做啤酒辅料的大米挤压膨化系统诸参数(模孔孔径、套筒温度、物料含水率、螺杆转速),对醪液的主要考察指标(麦汁醪液的总还原糖、过滤速度)的影响规律,指出挤压膨化大米做啤酒辅料的可行性。 相似文献
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This study was conducted to develop a ready‐to‐eat extruded food using a single‐screw laboratory extruder. Blends of Indian barley and rice were used as the ingredients for extrusion. The effect of extrusion variables and barley‐to‐rice ratio on properties like expansion ratio, bulk density, water absorption index, hardness, β‐glucan, L*, a*, b* values, and pasting characteristics of extruded products were studied. A central composite rotatable design was used to evaluate the effects of operating variables: die temperature (150–200°C), initial feed moisture content (20–40%), screw speed (90–110 rpm), and barley flour (10–30%) on properties like expansion ratio, bulk density, water absorption index (WAI), hardness, β‐glucan, L*, a*, b* values, and sensory and pasting characteristics of extruded products. Die temperature >175°C and feed moisture <30% resulted in a steep increase in expansion ratio and a decrease in bulk density. Barley flour content of 10% and feed moisture content of <20% resulted in an increased hardness value. When barley flour content was 30–40% and feed moisture content was <20%, a steep increase in the WAI was noticed. Viscosity values of extruded products were far less than those of corresponding unprocessed counterparts as evaluated. Rapid visco analysis indicated that the extruded blend starches were partially pregelatinized as a result of the extrusion process. Sensory scores indicated that barley flour content at 20%, feed moisture content at 30%, and die temperature at 175°C resulted in an acceptable product. The prepared product was roasted in oil using a particular spice mix and its sensory and nutritional properties were studied. 相似文献
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挤压加工参数对重组米生产过程及产品膨胀度的影响 总被引：3，自引：1，他引：2
为了考察重组米生产过程中挤压加工变量对几种系统参数与产品膨胀度的影响,试验以杂交籼米（9?718品种）为原料,利用响应面模型,以螺杆转速、进料速度、进料含水率以及末端机筒温度为输入变量,以挤压系统参数（物料温度、模头压强、扭矩、比机械能和产品含水率）和重组米膨胀度为响应变量,探索在重组米生产过程中加工变量与系统参数及产品膨胀度的关系。结果表明,压强、比机械能和产品膨胀度都受到4个挤压变量的显著影响,但是物料温度受进料速度影响不显著,马达扭矩受末端机筒温度影响不显著,产品含水率仅受进料含水率的显著影响。比机械能与螺杆转速正相关,与进料速度、进料含水率和末端机筒温度负相关。所得二次回归模型均拟合良好,建立的挤压数学模型可应用于重组米生产,为重组米工业化生产的过程预测和产品性质预测提供参考。 相似文献
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Twin‐screw extrusion of wheat flour and the effects on the flour proteins were studied using flour samples containing 9, 20, and 30% protein. Vital gluten containing 70% protein was used to achieve the flour protein levels. The three flour samples were extruded with a twin‐screw extruder at a combination of processing parameters (exit die temperatures of 120, 140, and 160°C, and screw speeds of 240, 320, and 400 rpm). Increasing extruder exit die temperatures resulted in increased sulfhydryl content of the 9 and 20% protein content flour samples, but appeared to have little or no effect on the 30% protein content flour sample. Similarly, disulfide content decreased, albeit disproportionately, following the same trend. Both sulfhydryl and disulfide contents of extruded samples were lower than those of the nonextruded samples and could imply denaturation of protein, aggregation through intermolecular disulfide bonds, or oxidation during extrusion processing. Total cysteine content of extruded samples decreased by ≈16% relative to nonextruded samples, but otherwise remained almost unchanged among all extruded samples. The loss of total cysteine in extruded samples could represent the generation of hydrogen sulfide, volatile organic compounds, or flavor compounds during extrusion. SDS‐PAGE analysis of total proteins showed a shift from the higher to lower molecular weight regions for certain protein bands. Both depolymerization and protein aggregation occurred at higher shear forces during extrusion. 相似文献
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Wheat flour with 0.3% (w/w) thiamin was extruded on a twin‐screw laboratory‐scale extruder (19‐mm barrel) at lower temperatures and expanded using carbon dioxide (CO2) gas at 150 psi. Extrusion conditions were die temperature of 80°C and screw speed range of 300–400 rpm. Control samples were extruded at a die temperature of 150°C and screw speed range of 200–300 rpm. Dough moisture content was 22% in control samples and 22 and 25% in CO2 samples. Expansion ratio, bulk density, WAI, and %WSI were compared between control and treatment. CO2 injection did not significantly increase expansion ratio. Bulk densities in the CO2 extruded samples decreased when feed moisture decreased from 25 to 22%. The products using CO2 had lower WAI values than products puffed without CO2 at higher temperatures. The mean residence time was longer in CO2 screw configurations than in conventional screw configurations. Thiamin losses were 10–16% in the control samples. With CO2, thiamin losses were 3–11% at 22% feed moisture, compared with losses of 24–34% at 25% moisture. Unlike typical high‐temperature extrusion, thiamin loss in the low‐temperature samples decreased with increasing screw speed. Results indicate that thiamin loss at lower extrusion temperatures with CO2 injection is highly dependent on moisture content. 相似文献
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An in‐line slit‐die viscometer (SDV) was used to measure the viscosity of a melt extrudate independently of the extruder operating conditions. The melt produced by extrusion of the corn grits followed a power law rheological model. The viscosity of the melt and extrusion parameters such as specific mechanical energy (SME), torque, and die pressure decreased with increasing moisture content. The degree of starch gelatinization increased when barrel temperature increased from 90 to 130°C. At temperatures higher than 130°C, most of the starch had gelatinized. The increase in barrel temperature, however, resulted in small changes in the apparent viscosity of the melt, until a maximum of ≈130°C. At a constant feed rate, SME increased and torque decreased when screw speed increased due to the shear thinning behavior of the melt. At a constant screw speed, the torque increased and SME decreased with increasing feed rate. This was due to a decrease in apparent viscosity of the melt at higher feed rates. SME is not an independent extrusion variable and should be used with caution either when predicting the effect of thermomechanical treatment of the product or as the key and only variable for controlling the food extrusion process. 相似文献