Study on the Vacuum Drying Model of Perilla Leaf by Microwave Method

2014 ◽  
Vol 664 ◽  
pp. 433-436
Author(s):  
Jiang Chang ◽  
Feng Xu ◽  
Guang Hua Wu ◽  
Xiao Feng Fu ◽  
Guang Li ◽  
...  

The drying rate is difficult to control for perilla leaf during the microwave vacuum drying process. Through scientific approaches, this paper made a research on the relationships between drying factors and drying rate, and established a kinetics model on microwave vacuum drying of perilla leaf. The model can predict the water content variations of perilla leaf during microwave vacuum drying, and provides a theory basis for packaging, storage and transportation for perilla leaf production.

Author(s):  
Yan Zhou ◽  
Haifeng Zhang

This paper introduced the design and research of spent resin conical dryer which was based on the analysis of the thermal decomposition characteristics of resins. The drying experiment of non-radioactive cation exchange resins and anion exchange resins was also carried out in this study. The result showed that the water content of resins reduced from about 55%(wt) to 8.5%(wt) and the volume reduction ration reached 2.17 with a drying end temperature of 90°C, which preliminarily verified the feasibility of the vacuum drying process and conical dryer device for treating radioactive spent resins.


2014 ◽  
Vol 1010-1012 ◽  
pp. 1783-1788 ◽  
Author(s):  
Jian Ping Zhang ◽  
Yong Hua Wu ◽  
En Qi Liu ◽  
Hui Song ◽  
Yong Li

The aim of this work was to find out an alternative drying process for semi-dry fermented sausages. Fermented sausages were subjected to hot air drying (HA) and microwave vacuum drying (MWV), respectively. The HA was carried out at 70 °C for 60 min. For MWV, three temperatures i.e. 30 °C, 40 °C and 50 °C were applied with pressure controlled at 80 kPa and microwave intensity at 6 kW for 2 min. After drying, the dehydration rates were determined immediately. The products were stored at room temperature until the end of experiment. The pH value, 2-thiobarbituric acid (TBA) and total volatile basic nitrogen (TVB-N) contents were measured at 0, 7, 14 and 28 days, respectively. In addition, the sensory properties were evaluated at 28 d. The results showed that compared to the HA, MWV could postpone the rise of pH value, TBA and TVB-N contents during the storage. Moreover, the sensory properties of MWV were better than that of HA, indicating that MWV would be a greatly promising drying process for semi-fry fermented sausages.


2011 ◽  
Vol 418-420 ◽  
pp. 94-101
Author(s):  
Hong Zhang ◽  
Lian Song Yu ◽  
Hua Zheng ◽  
Ying Feng ◽  
Xiao Ming Chen ◽  
...  

To enhance the product quality and production efficiency, we studied the kinetics of the microwave - vacuum drying of bleached shellac and optimized its technological process. Through the test, the drying curve, drying rate curve and drying constant of the bleached shellacs under different pressure were obtained and through the drying curve fitting, the drying model was obtained. And through the optimization test, the optimal conditions for the microwave - vacuum drying of bleached shellac were obtained, that is, pressure of 3000Pa, microwave power of 700W and drying time of 25min, then the products of color index of 0.9, water content of 0.0296 kg water / kg dry materials were obtained.


2009 ◽  
Vol 26 (2) ◽  
pp. 317-329 ◽  
Author(s):  
M. N. Berteli ◽  
E. Rodier ◽  
A. Marsaioli Jr

2013 ◽  
Vol 423-426 ◽  
pp. 746-749
Author(s):  
Samad Khani Moghanaki ◽  
Behnam Khoshandam ◽  
Mohammad Hosein Mirhaj

Convectional dryerswork at high temperature and usually lead to loss of quality for sensitivebiomaterial products (especially in nutrition). In this way the researchersfound the microwave power more effective and suitable for drying processes. Someof microwave drying advantages include the following: short drying time, highquality of product, low operating temperature, flexibility in producing widerange of products and easier process controlling. The article calculated themoisture content and drying rate during drying process. Microwave power, holdertray speed, dimension of samples, irradiation time were considered; under theseconditions experiments were done and the results show that microwave method hasmore advantages as comparing with convectional methods.


2020 ◽  
Vol 4 (4) ◽  
pp. 432-441
Author(s):  
Deni Setio Hadi ◽  
Mustaqimah Mustaqimah ◽  
Raida Agustina

Abstrak. Kunyit (Curcuma domestica VAL) adalah tanaman rimpang yang sangat populer sebagai rempah-rempah dan bahan obat, pemanfaatan kunyit dapat berupa kunyit segar,  kunyit kering, dan bubuk kunyit. Kunyit kering dapat memperpanjang masa simpan dan mempermudah pengemasan. Salah satu alat pengering yang dapat digunakan untuk mengeringkan kunyit adalah tray dryer. Penelitian ini menggunakan irisan kunyit sebanyak 4,5 kg, kemudian dikeringkan pada setiap variasi suhu yaitu 35ºC, 45ºC dan 55ºC. Perhitungan massa kunyit diukur tiap 30 menit sekali sampai bahan mencapai kadar air 5%. Parameter penelitian meliputi distribusi suhu, kelembaban udara, kecepatan aliran udara, penurunan bobot kunyit, kadar air, laju pengeringan, rendeman, kadar protein, dan uji diskriminatif serta uji hedonik terhadap warna, aroma dan tekstur. Hasil dari penelitian menunjukkan bahwa semakin tinggi suhu pengeringan maka semakin cepat proses pengeringan berlangsung. Pengeringan kunyit pada suhu 35ºC, 45ºC, 55ºC selama 390 menit, 270 menit dan 210 menit. Kelembaban relatif disetiap suhu yaitu 35ºC rata-rata sebesar 63,36%, suhu 45ºC sebesar 63,30% dan suhu 55ºC sebesar 62,25%. Rata-rata penurunan kadar air pada variasi suhu 35ºC, 45ºC dan 55ºC  sebesar 80,81% sehingga rata-rata kadar air akhir kunyit kering didapatkan sebesar 4,39%, dimana telah memenuhi  standar SNI untuk kadar air kunyit kering. Laju pengeringan tercepat pada suhu 55ºC rata-rata sebesar 2,38 %bk/menit. Rendemen tertinggi  bubuk kunyit terdapat pada suhu 35ºC yaitu sebesar 12,0%. Protein bubuk kunyit tertinggi pada suhu 55ºC sebesar 5,21%. Berdasarkan uji diskriminatif, yang mendekati warna dan aroma bubuk kunyit komersil adalah bubuk kunyit yang dikeringkan pada suhu 45ºC dengan skor 2 (sama). Berdasarkan hasil uji organoleptik hedonik panelis lebih menyukai warna bubuk kunyit yang dikeringkan pada suhu 45ºC dengan skor 5 (sangat suka) bila dibandingkan dengan warna bubuk kunyit yang dikeringkan pada suhu 35ºC dan 55ºC, dimana panelis hanya memberikan skor 4 (suka).Keywords: Drying Turmerics, Turmeric Powder, Tray Dryer.Abstract. Turmeric (Curcuma domestica VAL) Is a rhizome plant that is very popular as a spice and medicinal ingredient, the use of turmeric can be in the form of fresh turmeric, dried turmeric, and turmeric powder. Dry turmeric can extend its shelf life and simplify packaging. One dryer that can be used to dry turmeric is a tray dryer. This study used slices of turmeric as much as 4.5 kg, then dried at each temperature variation of 35ºC, 45ºC, and 55ºC. The calculation of turmeric mass is measured once every 30 minutes until the material reaches 5% water content. Research parameters include temperature distribution, air humidity, airflow velocity, reduction of turmeric weight, water content, drying rate, yield, protein content, and discriminatory test as well as a hedonic test on color, scent, and texture. The results of the study indicate that the higher the drying temperature, the faster the drying process will take place. Drying turmeric at 35ºC, 45ºC, 55ºC for 390 minutes, 270 minutes and 210 minutes. The relative humidity at each temperature is 35ºC at an averaging of 63.36%, a temperature of 45ºC at 63.30% and a temperature of 55ºC at 62.25%. The averaging decrease in water content at a temperature variation of 35ºC, 45ºC, and 55ºC was 80.81% so that the averaging water content of dried turmeric was obtained at 4.39%, which met the SNI standard for dry turmeric water content. The fastest drying rate at 55ºC averaging 2.38% bk/min. The highest yield of turmeric powder is at 35ºC, which is 12.0%. Turmeric powder is the highest protein at a temperature of 55ºC of 5.21%. Based on the discriminatory test, which approaches the color and scent of commercial turmeric powder is turmeric powder which is dried at 45ºC with a score of 2 (the same). Based on the organoleptic test results, panelists prefer the color of turmeric powder dried at a temperature of 45ºC with a score of 5 (very like) when compared to the color of turmeric powder dried at temperatures of 35ºC and 55ºC, where the panelists only gave a score of 4 (like).


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