农业工程学报
農業工程學報
농업공정학보
2014年
3期
277-284
,共8页
陈健凯%林河通%林艺芬%李辉%王志艳
陳健凱%林河通%林藝芬%李輝%王誌豔
진건개%림하통%림예분%리휘%왕지염
食用菌%干燥%优化%杏鲍菇%微波真空干燥%品质%能耗%参数
食用菌%榦燥%優化%杏鮑菇%微波真空榦燥%品質%能耗%參數
식용균%간조%우화%행포고%미파진공간조%품질%능모%삼수
fungi%drying%optimization%pleurotus eryngii%microwaves-vacuum drying%quality%energy consumption%parameter
为了提高杏鲍菇干制产品品质,降低干燥能耗,该文应用微波真空技术干燥杏鲍菇。采用三元二次回归旋转组合设计方法进行工艺参数优化试验,考察分析微波强度(X1)、物料厚度(X2)、腔体绝对压力(X3)因素对品质指标色差(Y1)、复水比(Y2)、氨基酸含量(Y3)和单位能耗(Y4)的影响及因子间交互作用对指标的影响;采用线性加权法,将多目标综合优化,确定干燥工艺的最优参数组合。结果表明:微波强度、物料厚度、腔体绝对压力对试验指标色差、复水比、氨基酸含量、单位能耗影响显著,物料厚度是影响色差的主要因素,物料厚度小于2 cm时,产品色泽较差;腔体绝对压力是影响复水比和氨基酸含量的主要因素,较小的腔体绝对压力有利于产品复水和减少氨基酸损失;微波强度是影响单位能耗的主要因素,高的微波强度,能耗较高,高的微波强度与较小的腔体绝对压力组合时,干燥能耗更高;杏鲍菇微波真空干燥高品质低能耗的最优工艺参数组合为微波强度12.5 kW/kg、物料厚度2.4 cm、腔体绝对压力18 kPa,此条件下干燥的产品品质优良,色泽洁白,色差L为78,复水性好,复水比为1.58,氨基酸破坏少,其值为473.1 mg/100 g,单位能耗较低,为9.3 kJ/kg。
為瞭提高杏鮑菇榦製產品品質,降低榦燥能耗,該文應用微波真空技術榦燥杏鮑菇。採用三元二次迴歸鏇轉組閤設計方法進行工藝參數優化試驗,攷察分析微波彊度(X1)、物料厚度(X2)、腔體絕對壓力(X3)因素對品質指標色差(Y1)、複水比(Y2)、氨基痠含量(Y3)和單位能耗(Y4)的影響及因子間交互作用對指標的影響;採用線性加權法,將多目標綜閤優化,確定榦燥工藝的最優參數組閤。結果錶明:微波彊度、物料厚度、腔體絕對壓力對試驗指標色差、複水比、氨基痠含量、單位能耗影響顯著,物料厚度是影響色差的主要因素,物料厚度小于2 cm時,產品色澤較差;腔體絕對壓力是影響複水比和氨基痠含量的主要因素,較小的腔體絕對壓力有利于產品複水和減少氨基痠損失;微波彊度是影響單位能耗的主要因素,高的微波彊度,能耗較高,高的微波彊度與較小的腔體絕對壓力組閤時,榦燥能耗更高;杏鮑菇微波真空榦燥高品質低能耗的最優工藝參數組閤為微波彊度12.5 kW/kg、物料厚度2.4 cm、腔體絕對壓力18 kPa,此條件下榦燥的產品品質優良,色澤潔白,色差L為78,複水性好,複水比為1.58,氨基痠破壞少,其值為473.1 mg/100 g,單位能耗較低,為9.3 kJ/kg。
위료제고행포고간제산품품질,강저간조능모,해문응용미파진공기술간조행포고。채용삼원이차회귀선전조합설계방법진행공예삼수우화시험,고찰분석미파강도(X1)、물료후도(X2)、강체절대압력(X3)인소대품질지표색차(Y1)、복수비(Y2)、안기산함량(Y3)화단위능모(Y4)적영향급인자간교호작용대지표적영향;채용선성가권법,장다목표종합우화,학정간조공예적최우삼수조합。결과표명:미파강도、물료후도、강체절대압력대시험지표색차、복수비、안기산함량、단위능모영향현저,물료후도시영향색차적주요인소,물료후도소우2 cm시,산품색택교차;강체절대압력시영향복수비화안기산함량적주요인소,교소적강체절대압력유리우산품복수화감소안기산손실;미파강도시영향단위능모적주요인소,고적미파강도,능모교고,고적미파강도여교소적강체절대압력조합시,간조능모경고;행포고미파진공간조고품질저능모적최우공예삼수조합위미파강도12.5 kW/kg、물료후도2.4 cm、강체절대압력18 kPa,차조건하간조적산품품질우량,색택길백,색차L위78,복수성호,복수비위1.58,안기산파배소,기치위473.1 mg/100 g,단위능모교저,위9.3 kJ/kg。
Microwave-vacuum experiments ofPleurotus eryngii were conducted in order to improve the quality of products and decrease the drying energy consumption. The effects of microwave power density (X1), material thickness (X2), absolute pressure chamber (X3) and the interaction of these three factors on color (Y1), rehydration ratio (Y2), amino acids (Y3) and unit energy consumption (Y4) were investigated in this study. The process parameters were optimized through the quadratic orthogonal rotary combination design with three factors and three levels. Linear weighting method was used to analyze comprehensive multi-objective optimization. The regression equations of four indexes were developed based on the experimental data and the optimal combination in process were obtained. The results showed that there were significant impacts of color, rehydration ratio, amino acids ofPleurotus eryngii and unit energy consumption from power density, material thickness and absolute pressure chamber. The major factor affecting on the color ofPleurotus eryngii was material thickness. The color ofPleurotus eryngii was poorwhen material thickness was less than 2 cm. The major factor affecting on rehydration ratio and amino acid ofPleurotus eryngii was absolute pressure chamber. The smaller absolute pressure chamber was beneficial to rehydration of driedPleurotus eryngiiand reduced the loss of amino acid of Pleurotus eryngiiduring drying. Microwave power density was the major factor affecting on the unit energy consumption. The energy consumption was high whenPleurotus eryngii was dried at high microwave power density. The combination of high microwave power density and small absolute pressure chamber could cause even higher energy consumption. The microwave power density of 12.5 kW/kg, material thickness of 2.4 cm and absolute pressure chamber of 18 kPa were the optimized parameters of microwave-vacuum dried Pleurotus eryngii with high-quality and low-energy consumption. Their product quality was excellent, the color was white (the value of color difference was 78), rehydration ratio (1.58) was appropriate, amino acids (473.1 mg/100 g) was less damaged , and unit energy consumption (9.3 kJ/kg) was lower.