HỘI NGHỊ KHCN TỒN QUỐC VỀ CƠ KHÍ - ĐỘNG LỰC NĂM 2017 Ngày 14 tháng 10 năm 2017 Trường ĐH Bách Khoa – ĐHQG TP HCM AMEASUREOFDRYINGTHEBAMBOOPOWDERINTHEPROCESSOFMANUFACTUREOFBAMBOOPLYWOODINVIETNAM Le Khanh Dien1, Tran Van Hung1, Vo Tuyen2, Nguyen Tan Hung2 Nguyen Thanh Nam2, Nguyen Huy Bich3 University of Technology, VNU-HCM, Vietnam National Key Lab of Digital Control and System Engineering, HCMUT, VNU-HCM, Vietnam Ho Chi Minh City Nong Lam University, Vietnam ABTRACT: Intheprocessof production ofthebamboo tree products; thebamboopowder is the principal material ina multiple bamboo products: chopstick, bamboo art plywood, absorbent of sweat mat… However, this kind ofpowder has a huge absorbing characteristic of water even mist inthe wet climate therefore theprocessof eliminating of water inbamboopowder is always requisite in order to keep in good condition The aim ofthe paper is to represent a design ofa typical drying machine ofbamboo tree powder that could be suitable to the domestic technology, salvage an unlimited natural energy inVietnamin order to save the energy and eliminating the pollution for the country The research could propose ameasureof saving energy for all kind ofdrying processes inthe future for domestic industry Keywords: dryingbamboo powder, natural energy, renewable energy, eliminating the pollution Introduction Bamboo is very popular ina large area in South East of Asia, especially inVietnam This evergreen tree is considered as natural fence that is unable to cross Bamboo is also a very raw material for wattle, canvas, basket, seat, chopsticks, village house frame and even boats… This paper represents ameasureofdryingbamboopowder with recommended productivity ofthe designed machine is 100 kg/h aBamboo tree Processof grinding trifling bamboo to powderThe following figures represent briefly theprocessoftheprocessof grinding trifling bamboo that were performed in CAD-CAM workshop ofthe 2National Key Lab of Digital Control and System Engineering (DCSELab), University of Technology, VNU-HCMC, Vietnam b After harvesting Trang 255 HỘI NGHỊ KHCN TỒN QUỐC VỀ CƠ KHÍ - ĐỘNG LỰC NĂM 2017 Ngày 14 tháng 10 năm 2017 Trường ĐH Bách Khoa – ĐHQG TP HCM c Trivial residue bamboo grinding machine d Bamboopowder Figure Processof production ofbamboopowder Design a typical dryingbamboopowder machine 1- Motor, 2- Reduction gearbox, 3- Chain engagement, 4- Bearing, 5- Rotating bamboopowder tank, 6- Exhalation chamber silo, 7- Central heating, 8- Fan, 9- Motor and gearbox Figure A system ofdrying general powderThe price ofbamboopowder will increase by the consumption of energy indryingprocess and a system ofdrying will engender a lot of pollution when gas, liquid fuel or rigid carburant are in central heating except electrical energy However, the price of electrical power is so high in comparison with the very low value ofbamboopowderIn this study we recommend to use direct thermal solar receivers that can satisfy all the given conditions 3.1 Analyze and selection a suitable system of direct solar a) Photo ofa typical dish/Sterling system There are many types of direct thermal solar receivers; each of them has its own Prod and Cond: - Circular disk has no concentric point, the heat cannot concentrated and themanufactureof circular disk is not practical (Figure 3a) - Parabolic circular disk has a focus but it is difficult to manufactureThe focus is a point so it is difficult to dry continuously a big amount ofbamboopowder - Parabolic troughs is selected because it has a focus line, practical and relatively easy to manufacture b) a 400-m2 dish system in Australia [1] Figure Parabolic circular disk has a focus Trang 256 HỘI NGHỊ KHCN TỒN QUỐC VỀ CƠ KHÍ - ĐỘNG LỰC NĂM 2017 Ngày 14 tháng 10 năm 2017 Trường ĐH Bách Khoa – ĐHQG TP HCM Parabolic trough is selected because its flexibility in manufacture, according to [8] the percentage of application of parabolic troughs solar system is inthe majority in application (Figure 4) Figure Reason of application of parabolic trough solar system 3.2 Parameters ofa parabolic troughs solar system Figure a) Mathematical parabola b) Schema ofthe designed drying system: axis ofthe system, 2: bamboo powder, 3: conveyor worm, 4: circular open trough absorber, 5: fixed frame 6: parabolic reflector Computing of heating inadryingpowderbamboo Wherein m0: the output mass ofbamboopowder after drying, 4.1 The necessary heat The quality ofbamboopowder is not depended on the uniform and homogenous ofthebamboo grain but it is depended on its dryness According to [1] the maximum moisture of wood in general is inthe range of 25% to 35% and the fungi cannot grow in wood when the moisture content is less than 20% Hence the designed system has the duty to decrease the moisture or increase the dryness ofbamboopowder from 5% to 15% The selected average value of 10% of moisture is accepted So the dryness 100 D= (mo - m1) 10%, mo m1: the input mass ofbamboopowder drying, before With the given productivity of 100 kg/h, the output mass ofbamboopowder after drying is 90kg and the mass of mixed water inside powder that is removed out ofbamboopowder is 10 kg/h According to [7]: Specific heat capacity of water liquid (25 0C) c= 4.1813 J/g.K = 4.1813 KJ/kg.K Specific heat capacity water vapor (1000C) =2.080 J/g.K = 2.080 KJ/kg.K According to [9] the temperature at collector can be greater than 3000C Eliminating all the loss of reflection, diffusion, transferring the temperature ofthepowder inside the worm tube cans greater Trang 257 HỘI NGHỊ KHCN TOÀN QUỐC VỀ CƠ KHÍ - ĐỘNG LỰC NĂM 2017 Ngày 14 tháng 10 năm 2017 Trường ĐH Bách Khoa – ĐHQG TP HCM than 1100 The necessary heat for alteration of 10 kg of water inside bamboopowder to steam and evaporate out ofpowderThe selected ambient temperature is 250C and the selected highest temperature when powder is out ofthe conveyor is 1100C W/m2 With the loss of parasitic energy and the coefficient lost heat is about 20%, the real solar heat is q=220x80%=176 W/m2 and the total area ofthe designed parabolic collector solar energy is A= Q/q=1000/176= 5.68 m2 Heat for alteration of 10 kg water from 25 to 1000 : 4.2 Design the parameters of parabolic trough reflector Q1 = m.C.t =10x 4.1813x (100-25)= 3135.975 kJ A parabolic trough solar system in Figure is selected to gain the area of 5.68 m2: Heat for alteration of 25 kg water at 1000 to steam at 1000: - The parameter reflector is made by a stainless steel sheet SUS304 with a dimension Q2 = m.C=10x2.080=20.8 kJ Heat for alteration of 10 kg water from 1000 to 1100: Q1 = m.C.t =10x 2.080 x (110-100)= 208 kJ Total necessary heat: Q= Q1 + Q2 + Q3=3364.775 kJ for 100 kg of initial bamboopowder per hour The total heat had to be received per second or the needed heat power Q=3364.775/3600= 0.93 kW For security we selected the total heat power that the parabolic trough have to provide to thebamboopowder is Q=1 kW According to [9] and [10] the direct energy on of 0.5x3000x2000 Thus the width ofthe sheet 0.5 mm and the area ofthe stainless steel reflector is 2000x3000=6 m2, bigger than the demanded area of 5.68 m2 The axial length is m and the parabolic circumference arc is m that allows the length of circular absorber trough which hold the conveyor worm is stable with roller bearings at ends The sheet is bended and assembled its back to a composite frame of 20 mm width that is considered as thermal isolator -The focus distance OF is f = 0.5 mm, the equation ofthe parabola in Cartesian coordinate system is very simple: surface ofthe earth at a rate of about q=220 Figure Mathematical parabola diagram, focus distance f =OF=0.5 m 4.3 Design the parameters of worm conveyor Trang 258 - The conveyor worm A with the diameter of 250 which is adjusted to be coaxial with the HỘI NGHỊ KHCN TOÀN QUỐC VỀ CƠ KHÍ - ĐỘNG LỰC NĂM 2017 Ngày 14 tháng 10 năm 2017 Trường ĐH Bách Khoa – ĐHQG TP HCM focus line (point F in Figure 6) ofthe parabolic reflector is assembled to the center line ofthe open top circular absorbers trough B via a couple of end flanges roller bearing C inthe Figure Selected length of trough and worm conveyor is 2000 mm (a bearing at a middle ofthe conveyor worm is no need), selected worm pitch is 250 mm hence there are about spiral pitches along the worm Figure Structure of conveyor bamboopowder absorber: a: Worm shaft b.Trough (solar receiver that is painted in black color outside) b End flange seft alignment roller bearing The parabolic reflector and the absorber are fixed each other and can rotate around a hint (F) 4.4 Orienting the axis of solar system to the Sun The Sun, the focus F and the vertex O ofthe parabolic solar system are always keep ina slightly straight line by the rotation motion of shaft F ofthe system The angular velocity ofthe system is equal to the one ofthe Earth That means: =2 radians/24 h= 2/(24x3600) 7.272e-5=0.00007272 rad/s rad/s= Or the rotating demanded angle ofthe system per minute = 0.1250 = 0.75’ This angle too small so we decided that it can be adjust time by time by hand in such a way that the shadow ofthe absorber F is at the vertex O ofthe reflector With the suitable direction of parabola axis, line rays from the Sun are considered from infinite and are parallel to the axis and reflex to the center of focus line or the absorber trough ACKNOWLEDGMENT This research is supported by DCSELAB and funded by Vietnam National University (Figure 7) The worm A is co-axis of trough B is activated by a motor to transport thebamboopowderinthe absorber open top tube All these above components are fixed together and with the parabolic trough All the system can be adjusted by hand to direct the parabola axis to the Sun The support is nailed to the earth and bears the system via the bearing A Conclusion The design ofdryingbamboopowder machine by direct solar energy is a suitable measureofdryingpowder that is practical and saving energy The design almost achieved and ready to be manufactured We hope that the designed will save energy and sustainable inthe protection of environment The ability ofmanufacture is enabling and inthe near future the automatic orientation to the Sun installation will be included to ensure the better performance ofthe system HoChiMinh City (VNU-HCM) under grant number GEN 2016.48.02.06 Trang 259 HỘI NGHỊ KHCN TỒN QUỐC VỀ CƠ KHÍ - ĐỘNG LỰC NĂM 2017 Ngày 14 tháng 10 năm 2017 Trường ĐH Bách Khoa – ĐHQG TP HCM REFERENCES [1] Jack Robinson RRC,”Determining acceptable moisture content inplywood sheathing”, Professonal roofing, April 1996 [6] I S Sintali, G Egbo and H Dandakouta “Energy Equations for Computation of Parabolic-Trough Collector Efficiency Using Solar Position Coordinates”, American Journal of Engineering Research (AJER) eISSN: 2320-0847 p-ISSN : 2320-0936 Volume-3, Issue-10, pp-25-33 www.ajer.org [7] Thermal capacity, Creative Commons Attribution-Share Alike 3.0 Unported http://creativecommons.org/licenses/bysa/3.0/ [1] “Direct Solar Energy”, Intergovernmental panel on climate Chanes, Contribution to Special Report Renewable Energy Sources (SRREN) [2] “Solar energy renewable & sustainable Energy”, Science & Technology, Stellenbosh University, Republic of South Africa [3] Dan Arvizu (USA) and Palani Balaya (Singapore/India) “Direct Solar Energy”, Cambridge University Press, Cambridge, United Kingdom and New York, NY, USA [8] Matthias Gunther, Michael Joemann, Simon Sambor “Parabolic trough technology”, Avanced CSP Technology, Enermena [4] S C Bhattacharya, S Kumar “Direct solar energy”, Renewable energy systems: direct solar energy- Direct Solar Energy [9] G.N Tiwari, Arvind Tiwari, Shyam “Handbook of energy solar theory, [5] Catalog No 787E, “Screw Conveyor Catalog & Engineering Manual” [10] “Solar energy”, National Energy Strategy, Executive Summary, 1991/1992 hand book and application”, Spinger Edition MỘT BIỆN PHÁP SẤY KHƠ BỘT TRE TRONG QUI TRÌNH CHẾ TẠO VÁN ÉP BẰNG TRE TẠI VIỆT NAM Tóm tắt Trong quy trình sản xuất sản phẩm từ nguyên liệu tre bột tre nguyên liệu chủ yếu cho nhiều loại sản phẩm tre đa dạng như: đũa tre, ván ép mỹ thuật làm tre, chiếu tre hút mồ hôi,… Tuy nhiên, loại bột lại có tính hút nước cao, hút sương mù thời tiết ẩm ướt Vì quy trình loại trừ nước bột tre ln ln vấn đề tiên để trì tình trạng khả dụng loại vật liệu Mục tiêu nghiên cứu trình bày cơng việc thiết kế chủng loại bột tre phù hợp với công nghệ nước, sử dụng nguồn lượng thiên nhiên vô tận Việt Nam nhằm tiết kiệm lượng tránh ô nhiễm cho môi trường Chúng hy vọng biện pháp tiết kiệm lượng tránh nhiễm nghiên cứu giúp tiết kiệm lượng cho loại máy sấy khác nước Từ khóa: sấy bột tre, lượng tự nhiên, lượng tái tạo, loại bỏ ô nhiễm Trang 260 ... system can be adjusted by hand to direct the parabola axis to the Sun The support is nailed to the earth and bears the system via the bearing A Conclusion The design of drying bamboo powder machine... hand in such a way that the shadow of the absorber F is at the vertex O of the reflector With the suitable direction of parabola axis, line rays from the Sun are considered from infinite and are... m1: the input mass of bamboo powder drying, before With the given productivity of 100 kg/h, the output mass of bamboo powder after drying is 90kg and the mass of mixed water inside powder that