An appropriate rice-based (ARB) biomass gasifier was designed and de-veloped for farmers’ use. The gasification properties of rice-based biomass were determined before doing the design. The gasifier was built using salvage petrol drums, metal bars and concrete as primary construction materials. It has a 30 cm-diameter reactor insulated with refractory cement. A 10 cm-o cross flow scrubber with 30 cm-thick packed-bed filter is used for conditioning the gas. The gas is converted to mechanical power with the use of a four-stroke-cycle, spark ignition engine commonly used by farmers. The gasifier was tested and u nderwent series of modifications and improvements. Performance test and evaluation showed that the gasifier performs satisfactorily as per design. Raw rice husk was found to have greater advantage as fuel for the gasifier than rice straw. It can drive sta-tionary agricultural machines such as a 4-in. pump, a 30-cm biomass chip-per, and a 20-cm rubber creeping mill. It can also power a 3-kWe AC gen-erator for lighting and a 60-Amp DC alternator for charging batteries. The entire system can be built at a cost of P90,000.00 (USD1 = PHP50) using local materials and skills. Analysis showed that the operating cost of the gasifier is only P94.15 per day. A savings o P244.94 per day can be derived against the use of purely gasoline fuel for the engine. Payback period is 1.22 years.
With the enactment of the Agricultural and Fishery Mechanization Act (AFMech) in 2014, the level of farm mechanization in the Philippines has increased from 0.52 hp/ha in the mid 90’s [
Rice-based biomass, consisting of rice husks and straws, is a potential source of energy to provide power for agricultural machinery [
Gasifier technology for biomass like rice husk has been developed ranging from a simple batch-type to a continuous-type reactor [
By using locally-available surplus-oil and -petrol drums commonly found along the roadsides outside Metro Manila, like Bulacan and Nueva Ecija, a gasifier can be made as simple as possible where even farmers and/or local people can build it themselves. There is no need for them to buy new engine because they can utilize their existing one by just adding pipes and valves in order to retrofit it to be able to utilize the gas they produced from the gasifier.
This study aimed to develop an appropriate rice-based biomass (ARB) gasifier as source of power for farm use. Specifically, it aimed to: 1) determine the gasification properties of rice-biomass required in the design of ARB gasifier, 2) design, build, and develop the gasifier that can run small spark ignition engines using locally available materials and skills in fabrication, 3) test and evaluate the performance characteristics of the gasifier as well as its ability in powering small agricultural machines, and 4) analyze the operating cost and determine the payback period of the gasifier.
Rice husk is around 20% of paddy harvested while rice straw is 5 times more than rice husk [
There are different methods of gasifying rice husks which can also be adopted for rice straw. These include: fixed-bed, moving-bed, and fluidized-bed gasification operating either by downdraft or updraft mode [
The University of California (UC) Davis designed and developed a small-scale rice husk gas producer for engine operation in mid 80’s [
Moreover, a moving-bed downdraft rice husk gasifier that allows continuous operation in a single reactor was developed in the Philippines [
straws as to their potential as fuel for the gasifier. Fresh or new rice husks obtained from a rice mill near PhilRice was used as samples; whereas for rice straw, threshed panicles and stubbles left in the field for a month were used. The rice straw samples were cut into small sizes of around 6- to 10-mm in length. All the samples were placed in a room for a week to allow their moisture to equilibrate before they were subjected in the test rig. Determination of the gasification properties of the different samples were carried out at an airflow rate in which burning flames are visibly observed at the burner of the test rig. The data needed such as weight of samples and char produced, operating time, temperature of gas and temperature at the fuel bed, velocity of air entering the reactor, as well as static pressure were all gathered. Parameters analyzed include: 1) Bulk density; 2) Air/Fuel ratio; 3) Superficial gas velocity; 4) Specific gasification rate; 5) Specific draft; 6) Reactor bed temperature; and 7) Gas temperature. The percentage composition of CO, H2, CH4, CO2, CnHm, O2, and lower heating value of gas were also determined.
A conceptual design of the ARB gasifier was prepared considering the following criteria: 1) primary materials for the gasifier unit should utilize 50 liter- and 200 liter-capacity salvage petrol drums; 2) plastic pipes must be used to convey the gas; 3) use of GI pipes, bars and sheets must be minimal and use of locally-available standard parts of the machine; 4) tools for fabrication of the gasifier must be readily available; 5) standard parts, such as pump and suction blower, must be available from the local suppliers; and 6) 16 - 22 Hp single-piston spark-ignition engine commonly available in the farm must be used.
The conceptual design and calculations for the size of the gasifier components were prepared including the drawings and list of materials to build a prototype unit.
The prototype unit of the gasifier was fabricated based on the design drawing provided to the shop technician at Rice Engineering and Mechanization Division at PhilRice Central Station. Regular monitoring was done to ensure that the gasifier is fabricated according to the design drawing. After each part was built, they were all coupled together to complete the entire unit for series of functional tests, modification and improvement.
Performance testing and evaluation of the gasifier built were carried out in selected field sites. The gasifier was run with only the pump and the blower are attached to it as load to determine its performance characteristics. Different machines were attached to see whether the gasifier is capable in driving the loads. The following were determined during the tests: 1) Amount of fuel used; 2) Operating time; 3) Gas flow rate; 4) Temperature at different locations in the system; 5) Engine speed and sound level; 6) Gas quality (CO, H2, & CH4); 7) Output of the machine coupled to the engine; and 8) Amount of char produced.
The weight of fuel and the weight of char produced were measured using a 20-kg spring balance. A probe-type moisture meter was used in determining the moisture content of the samples. The time to ignite the fuel and to generate combustible gas as well as the total time of operation were recorded using a Digital Stopwatch. Temperature at the different sections of the gasifier was taken using a Type-K thermocouple-wire sensors attached to a digital thermometer (EXTECH Thermocouple Datalogger Model TM500) and by a RICK Dial-type Thermometer (0˚C - 150˚C). The volumetric flow rate of gas entering the engine was determined by measuring the velocity of the gas in the pipe leading to the engine using EXTECH Hot Wire Thermo-anemometer Model SDL 350 multiplied by the cross-sectional area of the pipe. The composition and the heating value of the gas entering the engine were also taken using Amperis Gas Analyzer Transdox 5100B. In measuring the water flow rate at the scrubber, a rotary flow meter was attached to the intake pipe of the scrubber. The speed of the pump, of the blower, and of the engine drive shaft were all taken using an EXTECH Laser Photo Tachometer Model RPM33. The sound released by the engine was measured at 1.5-m high and at 1-m distance from the engine muffler using an AZ Digital Sound Level Meter Model 8928. The pH measurement of water in the pond was taken with the use of AZ pH meter 8684.
From the data gathered, the following parameters were analyzed: 1) Fuel Consumption Rate; 2) Specific Gasification Rate; 3) Gas Flow Rate; 4) Fuel/Gas Ratio; 5) Fire Zone Rate; 6) Superficial Gas Velocity; 7) Water/Gas Ratio; and 8) Percentage Char Produced.
Rice Husks | Rice Straw Panicles | Rice Straw Stubbles | |
---|---|---|---|
Bulk Density, kg/m3 | 101 - 104 | 45 - 51 | 57 - 59 |
Air-Fuel Ratio, kg air/kg fuel | 0.88 - 1.09 | 0.56 - 0.68 | 0.97 - 1.08 |
Superficial Gas Velocity, cm/sec | 2.26 - 4.86 | 1.47 - 1.86 | 2.12 - 3.32 |
Specific Gasification Rate, kg/hr-m2 | 115.8 - 199.9 | 117.3 - 123.4 | 120.3 - 138.2 |
Specific Draft, mm H2O/m | 6.22 - 19.40 | 2.74 - 2.86 | 4.48 - 9.40 |
Reactor Fuel-Bed Temperature, ˚C | 416 - 477 | 625 - 735 | 625 - 738 |
Gas Temperature, ˚C | 247 - 259 | 218 - 268 | 223 - 314 |
Char Produced, % | 28.6 - 31.3 | 14.3 - 27.7 | 27.2 - 30.3 |
bulk density, which is the determining factor for the size of the reactor of the gasifier. Rice husk has higher bulk density which is almost double of that of rice straw panicles and rice straw stubbles with 101 to 104 kg/m3, 45 to 51 kg/m3 and 57 to 59 kg/m3, respectively. In terms of the amount of air required per amount of fuel to be used, results showed that rice husk uses more air (0.88 to 1.09) to gasify than rice straw (0.56 to 1.08). The superficial velocity of gas in the fuel bed, which is an indicator of hole formation in the fuel bed, ranges from 2.26 to 4.86 cm/sec for rice husk, from 2.12 to 3.32 cm/sec for rice straw stubbles, and from 1.47 to 1.86 cm/sec for rice straw panicles. Holes formation in the fuel bed must be prevented during operation for it reduces the quality of gas produced. The specific gasification rate, which is usually used in determining the diameter of the reactor, is higher for rice husk than that for rice straw samples. Rice husks operate at a specific gasification rate at a range of 115.8 to 199.9 kg/hr-m2 while for rice straw panicles and stubbles are at the range of 117.3 to 123.4 kg/hr-m2 and 120.3 to 138.2 kg/hr-m2, respectively. In terms of specific draft, which is used to determine the pressure draft requirement of the blower for the gasifier, rice husk samples obtain a higher value (6.22 to 19.40 mm H2O per meter) than that of rice straw samples, which is 2.74 to 2.86 mm H2O per meter for rice straw panicles and 4.48 to 9.40 mm H2O per meter for rice straw stubbles.
With regard to the temperature at the fuel bed in the reactor, rice husk has lower temperature (416˚C to 477˚C) than rice straw samples (625˚C to 735˚C, and 625˚C to 738˚C rice straw panicles and rice straw stubbles, respectively).It implies that rice straws, having low bulk density, burn easily than rice husks. Moreover, the slightly higher temperature of the gas leaving the reactor with rice straws (218˚C to 314˚C) than with rice husks (247˚C to 259˚C) is likewise indicative of more burning of rice straw samples as compared with rice husk samples. As a result, lesser amount of char produced is obtained for rice straw panicles (14.3% to 27.7%) and for rice straw stubbles (27.2% to 30.3%) than that of rice husks (28.6% to 31.3%).
Results in the composition of gases derived from the samples tested,
The design development of the gasifier unit underwent step-by-step processes until the final ARB gasifier was fully developed.
Rice Husk | Rice Straw Panicles | Rice Straw Stubbles | |
---|---|---|---|
Carbon Monoxide (CO), % | 13.20 - 14.41 | 6.08 - 7.81 | 8.81 - 8.88 |
Methane (CH4), % | 1.43 - 1.88 | 1.19 - 1.58 | 1.62 - 1.81 |
Hydrogen (H2), % | 6.10 - 6.13 | 1.35 - 2.94 | 3.12 - 4.11 |
Carbon Dioxide (CO2), % | 11.70 - 12.09 | 12.81 - 13.15 | 12.00 - 13.03 |
Hydro Carbon (CnHm), % | 0.04 - 0.06 | 0.15 - 0.16 | 0.10 - 0.20 |
Oxygen (O2), % | 0.61 - 0.79 | 4.20 - 5.12 | 3.54 - 4.69 |
Lower Heating Value, kcal/m3 | 695 - 763 | 346 - 470 | 527 - 535 |
The reactor serves as the gas generating component of the system. It is where rice-based biomass undergoes thermochemical reaction to produce combustible gases which can be used as fuel for an internal combustion engine. Two 35 cm-f by 60 cm-long grease drums are used as inner cylinder for the reactor. A locally-mixed refractory cement was used as insulation, with 5-cm thickness, for the drums. On the other hand, two petrol drums (200-liter cap per drum), each having 60-cm f by 90-cm high, are used as outer cylinder for the reactor. During development, flanges are provided for the drums to facilitate repair and improvement work. The inner cylinder drum is centrally welded at the top portion of the outer cylinder drum. A 2½-in.f by 20-cm high GI pipe is welded at the annular space between the inner and outer cylinders serving as gas outlet. Beneath the inner cylinder is a char discharge mechanism designed to temporarily hold burned rice husks in pockets for a gradual discharge of the char during operation.
The gas conditioning device serves as the cleaning, cooling and storage component for the gas produced from the reactor. It is made of two drums welded end-to-end having 60-cm φ and 1.8-mtotal height. A cross-flow scrubber, which is attached to the reactor, is installed at the top of the gas conditioning cylinder. It is made of a 4 in.-f by 120 cm-high pipe serving as outer casing and a 2½-in. pipe, with 3 mm-f holes at the periphery, as inner casing. Water is forced to the annular space of the pipes by a ½-in. gear pump to create spray water for the gas. A 6 mm-f perforated sheet is installed at the middle of the gas conditioning cylinder to hold the filter materials, which is made of crushed stones (6 mm- to 10 mm-f), to mechanically screen the gas. The gas exits from the top of the gas conditioning cylinder through a 2½-in.f pipe leading to a smaller drum serving as gas storage and, at the same time, to allow the water that goes with the gas to drip.
The water cooling pond, on the other hand, is where the reactor and gas conditioning device seats through an angular support frame. The water in the pond seals the bottom end of the reactor and quenches burning of discharged char. It is constructed on ground using pure concrete or, in some cases, using metal sheets with 120 cm-wide by 150 cm-long and 50 cm-deep dimension.
The power generating device converts the gas produced into mechanical power with the use of 16-hp, 17-hp, or 22-hp, 4-stroke-cycle, spark ignition engine. The engine crankshaft drives a 1¼-in. shaft with the use of a chain coupler where the suction blower and gear pump are being driven by means of belt and pulley. The blower is directly coupled to a 2 in.-f plastic hose to suck the gas from the reactor and from the gas conditioning unit and deliver it into the intake manifold of the engine.
are removed when the gas passes through spray water. The spray water also reduces the temperature of the gas before it enters the intake manifold of the engine. Solid and liquid particles that go with the gas are filtered as the gas passes through the layers of crushed stones. The gas then exits from the gas conditioning unit and to the gas storage to further remove some water from it before it enters the engine. The power produced by the engine is used to provide the parasitic load as well as to drive stationary agricultural machines.
Measurement of the noise level emanating from the engine muffler ranges from 87.2 to 92.4 dB. These values indicate that there is no need to install a silencer in order to deaden the noise of the engine. The pH values in the water pond, measured at the start and at the end of operation, range from 7.6 to 9.0 and from 7.6 to 8.4, respectively, indicating that there is a slight change in the acidity of water. Only 1 operator is required to operate the entire system which includes loading of fuel and unloading of char.
Run 1 | Run 2 | Run 3 | |
---|---|---|---|
Weight of Fuel Used (kg) | 16.0 | 17.1 | 16.5 |
Moisture Content (%) | 13 | 9 | 11 |
Start-Up (min) | 5 | 6 | 5 |
Gas Generation Time (min) | 10 | 11 | 5 |
Total Operating Time (hr) | 1.46 | 1.63 | 1.55 |
Shaft Speed (rpm) | |||
Engine | 2445.5 | 2631.7 | 2633.9 |
Blower | 5813.5 | 7238.3 | 6804.5 |
Pump | 866.9 | 1081.4 | 1081.8 |
Volume of Gasoline Used (liter) | 0.8 | 0.5 | 0.4 |
Sound (dB) | 92.4 | 91.8 | 87.2 |
pH Start | 9.0 | 8.0 | 7.6 |
End | 8.4 | 7.6 | 7.7 |
Number of Operator | 1 | 1 | 1 |
Fuel Consumption Rate (kg/hr) | 10.91 | 10.47 | 10.65 |
Specific Gasification Rate (kg/hr-m2) | 154.34 | 148.12 | 150.67 |
Gas Flow Rate (m3/hr) | 5.47 | 7.34 | 7.17 |
Fuel/Gas Ratio (kg fuel/m3 of gas) | 1.99 | 1.43 | 1.48 |
Fire Zone Rate (cm/min) | 0.88 | 0.99 | 1.17 |
Superficial Gas Velocity (cm/s) | 1.56 | 2.10 | 2.05 |
Water/Gas Ratio (liter/m3 of gas) | 37.04 | 58.38 | 45.86 |
Gasification Efficiency (%) | 13.15 | 18.81 | 17.87 |
Run* | CO (%) | H2 (%) | CH4 (%) | CO2 (%) | O2 (%) | LHV (MJ/m3) |
---|---|---|---|---|---|---|
1 | 9.372 | 3.378 | 3.958 | 5.038 | 7.564 | 2.976 |
2 | 9.412 | 4.008 | 3.902 | 4.418 | 8.380 | 3.044 |
3 | 9.592 | 4.502 | 3.476 | 4.490 | 8.278 | 3.008 |
*Average of the samples of gases taken at the start, middle, and end of the operation.
Machine | Engine | Fuel | Load | Fuel Consumption Rate (kg/hr) | Time Operated (hr) |
---|---|---|---|---|---|
Centrifugal Self Priming Pump 4 in. | Yamamoto 17 hp | Rice husk | Q = 30.27 m3/hr @ H = 1.2 m | 7.3 | 4.0 |
Yamamoto 17 hp | Rice Straw | Q = 15.71 m3/hr @ H = 1.1 m | 8.5 | 0.5 | |
Biomass Chipper 30 cm Disk | Daikin 16 hp | Rice husk | 53 kg of madre de cacao twigs and branches (4 mm to 20 mm D) per hour | 10.1 | 2.1 |
Daikin 16 hp | Rice Husk | 16.9 kg of ipil-ipil twigs and branches (6 mm to 10 mm D) per hour | 11.5 | 2.5 | |
Rubber Creeping Mill Double roller 15 cm D | Yamamoto 17 hp | Rice husk | 86 kg of treated rubber latex per hour | 9.8 | 3.7 |
AC Generator 3 kWe | Daikin 16 hp | Rice husk | 300 to 500 watts | 12.0 | 2.7 |
Daikin 16 hp | Rice husk | 300 to 500 watts | 18.7 | 2.3 | |
AC Generator 3 kWe | Robin 22 hp | Rice husk | 450 to 710 watts | 8.3 | 4.1 |
Robin 22 hp | Rice husk | 450 to 710 watts | 8.5 | 4.0 | |
DC Alternator 12 volt, 60 amp | Daikin 16 hp | Rice husk | 35 Amp in charging 12 volt, 100 AH gel type battery | 11.2 | 1.5 |
to produce chipped ipil-ipil at a rate of 16.9 kg per hour with rice husk consumption of 11.5 kg per hour for a running period of 2.5 hours. Powering a rubber creeping mill to produce rubber blankets showed that the gasifier can drive the machine using 16-hp Yamamoto engine at a rate of 86 kg of treated rubber latex per hour. The gasifier consumed 9.8 kg of rice husk per hour for 3.7 hours of operation.
For micro electrical power generation, a 3-kWe AC generator with 16-hp Daikin engine can generate 300- to 500-watts electricity with rice husk consumption of 12.0 kg per hour in the first run for 2.7 hours operation and 18.7 kg per hour in the second run for 2.3 hours operation. Using a two-cylinder 22-hp Robin engine, the 3-kWe AC generator can generator 450- to 710-watts power with rice husk consumption of 8.3 kg per hour for 4.1 hours in the first run and 8.5 kg per hour for 4.0 hours in the second run. Using the 16-hp Daikin engine in driving a 12-Volt, 60-Amp DC alternator, that is commonly used in charging car batteries, can generate 35 amperes to charge a 12 volt, 100-AH gel-type, maintenance-free car battery with rice husk consumption of 11.2 kg for a period of 1.5-hour test.
Gasifier Engine | Gasoline Engine | |
---|---|---|
Investment Cost | 90,000.00 | 25,000.00 |
Fixed Cost (P/day) | ||
Depreciation 2/ | 31.70 | 8.81 |
Interest on Investment 3/ | 8.45 | 2.35 |
Repair and Maintenance 4/ | 3.52 | 0.98 |
Insurance 5/ | 1.06 | 0.29 |
Sub-Total | 44.74 | 12.43 |
Variable Costs (P/day) | ||
Rice Husk Fuel 6/ | 40.00 | - |
Gasoline 7/ | 6.75 | 324.00 |
Engine Oil 8/ | 2.67 | 2.67 |
Sub Total | 49.42 | 326.67 |
Total Costs (P/day) | 94.15 | 339.09 |
Cost per hour | 11.77 | 42.39 |
Savings per Day | P244.94 | |
Payback Period 9/ | 1.22 years |
1) Complete set; 5 years life span. 2) Straight line with 10% salvage value. 3) 24% of the investment cost. 4) 10% of the investment cost. 5) 3% of the investment cost. 6) P1.0 per kg of rice husks @ 1 sack per hour consumption. 7) 0.9 liter per hour @ P45/liter; for gas producer―10 min gasoline start-up per day. 8) P200.00 per liter @ 1 liter per engine-oil change every 600 hours. 9) 25 days per month for 12 months per year.
The ARB gasifier was successfully developed to provide farmers a source of power for their agricultural machines. The gasifier can also drive a small AC generator and a DC alternator to produce electricity for energizing farm houses, especially those in off-grid regions. The use of rice husks as fuel offers more advantage in the present unit because of its properties that is highly suitable for gasification. Rice straw can also be gasified; however, there is a need to further resize it to make it suitable as fuel for the gasifier.
Coupling other agricultural machines like micromills, small threshers, axial fan (that is used in a 3-ton flatbed dryer), and many others are encouraged to further explore the applicability of the gasifier.
We would like to thank PhilRice for supporting this study to develop a gasifier suitable for our farmers. The Approtech Enterprises in San Rafael, Bulacan and FJC Agro industries in Zamboanga Sibugay for providing the area and facility to tests and evaluate the machine. Above all, to the Almighty God for the wisdom and strength He gave in coming up with the appropriate gasifier design.
The authors declare no conflicts of interest regarding the publication of this paper.
Belonio, A.T., Regalado, M.J.C. and Castillo, P.R. (2018) Development of an Appropriate Rice-Based Biomass Gasifier as Source of Power for Farm Use. Open Access Library Journal, 5: e5054. https://doi.org/10.4236/oalib.1105054