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Research Detail

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Dr. Md. Arefin Kowser*
Department of Mechanical Engineering, DUET, Gazipur, Bangladesh

Dr. Hasan Mohammad Mostofa Afroz
Department of Mechanical Engineering, DUET, Gazipur, Bangladesh

Nayeem Md. Lutful Huq
Department of Mechanical Engineering, DUET, Gazipur, Bangladesh

Md. Khaled Khalil
Department of Mechanical Engineering, DUET, Gazipur, Bangladesh

Bangladesh is an agriculture-based developing country. A huge amount of rice husk is produced from paddy which creates a significant disposal. Although some rice husks are used as fuel for cooking, boiling paddy, electricity generation, and other purposes, but in most of these applications the maximum energy loss occurs due to inefficient burning process. To utilize maximum energy, rice husks should be burned properly. Rice husk gasification is one of the prior solutions where rice husk is burned properly for the utilization of maximum energy. In the present work, a down draught rice husk gasifier is fabricated, where the reactor is constructed to carry out a variety of chemical reaction. In the reactor, air is passed through rice husk at a controlled velocity for the partial combustion which produces a continuous flow of gas of usable form of energy. In this method once the processes is started it can be kept running as long as needed. The burnt solid waste is removed automatically after a certain period. As it gives efficient energy conversion it leaves a less environmental impact. The temperatures at different positions of gasifier are measured by K type thermocouples. The produced gas has been cooled by a radiator to 50°C to measure its flow rate and calorific value. Gasification tests have been conducted with varying air flow rates and fuel feed rates. The typical wall temperature of gasification process was about 400-450°C. The producer gas had an average temperature of 600-800°C and the pick heating value was 3.9MJ/m3 to 4.5MJ/m3.

  Environment Friendly, Continuous Flow Gas Generation, Fluidized Bed Rice Husk, Saw Dust Gasifier
  Department of Mechanical Engineering, DUET, Gazipur, Bangladesh
  
  
  Resource Development and Management
  Bio-gas

This paper is constructed as it begins with the introduction to the system and its background that leads to the objective of the work. After that it describes the methodology that describes the chemical processes, fabrication of the system, operation of different parts, waste handling method etc. and concludes with data acquisition for performance analysis. Then the paper proceeds to results and discussion which deals with different observations, performance analysis, positive and negative aspects of the method etc. and finally it is concluded with the concluding remarks and future recommendations.

A significant amount (20%) of the paddy is rejected from the rice mills which is the rice husk. Thus 132 million tons of rice husk were wasted in the year 2008 mostly by burning them in the open field. Yet the rice husk has an attractive calorific value which can be used by reclaiming it from those waste materials.

2.1 Characteristics of Rice Husk An inherent quality of the rice husk is that it doesn’t ignite and burn easily and to do that one needs to blow air through the husk. It also has to more positive qualities that it resists the moisture to get into it and cannot be decomposed with fungal attach. Thus this is often used as a good insulation material. Silica (SiO2 ) content in rice husk is very high therefore it decomposes over a long period of time if left alone in the open field. The rice husk is bulky and dusty which makes it less affordable for handling. Having an angle of repose of about 40°-45° makes it fluent through the feed hoppers. Because of its low bulk density (70-110 kg/m³, 145 kg/ m³ when vibrated or 180kg/m³ in form of pellets) a large storage capacity by volume is required for transport which leads to an uneconomical situation. As mentioned earlier because of its good calorific value (3410 kcal/kg) it is an attractive option for renewable energy research.

2.2 Fabrication The gasifier was fabricated using the available materials in Bangladesh so that the system can be constructed at any corner of the country economically. The complete design of rice husk gasifier is shown in Figure 01.

2.4 Chemical Reaction Occur into Gasification System There are different reaction zones where different types of reactions take place. In the oxidation zone: C + O2 = CO2+ 401.9 kJ/mol (1) H + O2 = H2O + 241.1 kJ/mol (2)

3. FABRICATION The fabrication consists of preparing and assembling the major parts of the gasifier. It takes different types of metal working, welding, electrical wiring, programming etc.

3.2 Description About Individual Parts The following sections describe some technical details of the individual parts of the gasifier. However, some of these consists of some smaller components. 3.2.1 Fuel feeding system The feed hopper is a conical part that serves as the temporary storage for rice husk. It is located on the top of reactor. This device is provided with a door that can be opened for easy disposal of rice husk. The hopper has a capacity of 15kg which is shaped like a funnel, works as a supplier and a reservoir. 3.2.2 Air supply system Two blowers (7.08m3 /min) work as the air supply unit for the reactor. These blowers are accompanied by pressure valve, main valve, bypass valve, and supply pipe. The blower is equipped with 25µ filter to clean the inlet air from dust particles, water etc. The blower-1 is used to supply air to the after burner, while blower-2 is used carry the bed material (char) away.

3.2.3 Start-up system Like all other start-up systems the start-up burner starts up the initial burning of the rice husk. It works by a spark plug. After the air supply and the ignition systems are turned on the start-up unit comes into play. The rice husk needs to be combusted below 800°C as well as hot spots or localized high temperatures are not expected. Which, unfortunately, in practice (in directly fired furnaces/ gasifiers) is not possible. This requires a large grate area and quick dissipation of heat. 3.2.4 Reactor The operation of the gasifier leads to a very high temperature inside the reactor resulting in much lower amount of CO2, also known as the greenhouse gas. This ranges from 5 to 15% which is almost 50% of the amount produced by direct combustion. Other quantities are; heating value: 1200 to 1400 kcal/m3, black carbon content: 10 to 50 gm/m3 , and tar content: 56 to 100 mg/m3.

3.2.5 Char chamber The char is deposited in char chamber. The temperature in this zone is about 50°C to 87°C. It is produced in the gasifier and is completely black, which is good for soil conditioning. Rice husk contain about 75% organic volatile matter and the balance 25% of the weight of this husk is converted into ash during the burning process which is known as char or rice husk ash (RHA). This RHA in turn contains around 85% - 90% amorphous silica. 3.2.6 Scraper The scraper is one of the most important elements in this set up. Here it is used to remove the char from the combustion chamber and driven by a dc motor that rotates after every five minutes. It is made of a shaft and a net. The shaft is coupled with a motor by a chain sprocket arrangement. The net should have ability to resist high temperature and the weight of a mass of about 15 to 20 kg. The scrapping system arrangement of the fabricated gasifier, which includes a motor controlled by timer.

  DUET Journal Vol. 3, Issue 1, December 2017
  
Funding Source:
1.   Budget:  
  

There are seasonal, geographical distribution and other variables in the availability of conventional energy sources in Bangladesh. The CFRHG technology clearly demonstrates that rice husk and sawdust can be efficiently gasified in a continuous mode following the principle of a moving bed inverted-downdraft technology. The use of scraper eliminates the problem of char clogging during operation. The technology can provide more benefits to the users, particularly in terms of convenience of operation and cost. It does not require advanced knowledge and high tech component and equipment for the fabrication; thus, it can easily be built using locally available resources and manpower. It also addresses the environmental aspect, since it is considered a clean technology based on black carbon and CO2 emissions, which are basically low. The by-products can be further used as valuable commodity products for the agriculture and construction sectors. Sawdust is suitable for gasification. Thus eight types of sawdust was used to determine the biomass characteristics of saw dust as solid biomass fuel. The temperature of different zones of gasifier are determined by the thermocouples. The temperature of the drying zone was 75°C–85°C, at temperatures 250°C–500°C, pyrolysis of the biomass fuel starts. A burning (oxidation) zone is formed at the level where oxygen (air) is introduced. Reactions with oxygen are highly exothermic and result in a sharp rise of the temperature up to 800°C–1400°C. The products of the oxidation zone (hot gases and glowing charcoal) move downward into the reduction zone. These reactions are endothermic so the gas temperature decreases (approx. 600°C–700°C). Temperature is maximum in the combustion chamber is 800°C–1400°C and the outer cover temperature of the reactor is about 500°C–700°C. Flame temperature of the gas is 450°C–620°C. The gas temperature is different with different inlet air velocity. Heating value of different sawdust are different. Heating value of mango wood is lower and the highest is jack fruit while the other samples varies slightly with each other. Chemical analysis shows that combustible gas produced by mango tree is the list while others are almost same with good percentage. When excess air is small in amount, the combustible gas composition is good with stable flame. Finally, it is recommended that less air velocity is required to achieve continuous flow of combustible gas production and better performance of the gasifier. Experimental value of ash content was different (about 5.7% to 7.69%) for sample of sawdust because of moisture content and combustion efficiency of the gasifier. The principle economic advantage of wood burning systems is that wood fuel is usually less expensive than competing fossil fuels.

  Journal
  


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