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Raw materials: rice husk, straw, herb, film, coconut shell
Advantages: fixed carbon, reproducibile, high volatile, low SO2 emmission, zero CO2 emmision
Raw materials: rice husk, straw, herb, film, coconut shell
Main energy: biomass black carbon, biomass wood vinegar
Biomass gasification power plant: capacity from 200kw to 3000kw, 1kg woody biomass generate 1kw electricity, 1kw woody biomass produce 2-3m3/h syngas, syngas heat value 1100-1500kcal/m3.
Applicable raw materials: a wide range of raw materials, such as straw, wood chips, rice husk, palm shell, bagasse and other agricultural and forestry wastes
particle size: 30-50mm, water content: less than 20%
Serial Number | Project | Sub Option | Quantity (Kg/H) | Unit Price (Yuan/Kg) | Consumption (Yuan/Day) | Consumption (Ten Thousand Yuan/Year) | Consumption (Ten Thousand Yuan/Year) | Total |
1 | Consume | Wood Chips | 2000 | 0.3 | 14400 | 43.2 | 432 | 432 |
2 | Output | Biomass Charcoal | 400 | 0.8 | 7680 | 23.04 | 230.4 | 311.04 |
Wood Tar | 40 | 0.8 | 768 | 2.304 | 23.04 | |||
Wood Vinegar | 100 | 0.2 | 1920 | 5.76 | 57.6 | |||
Annual Expenditure: 432-311.04=1.2096 Million Yuan | ||||||||
Traditional Energy | Monthly Net Profit After Saving (Ten Thousand Yuan) | Monthly Net Profit After Saving (Ten Thousand Yuan) | ||||||
Diesel Fuel | 288.13-12.1=276.03 | 2760.3 | ||||||
Heavy Oil | 218.28-12.1=206.18 | 2061.8 | ||||||
Natural Gas | 177.66-12.1=165.56 | 1655.6 |
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(2018) Suntivarakorn et al. Energy Reports. This article focused on production cost of pyrolysis oil production of Napier Grass in Circulating Fluidized Bed Reactor (CFBr) which sand was used as bed mahaiqial. The Napier grass was converted to pyrolysis oil by using fast pyrolysis process. The rea
Fast pyrolysis is applied to convert biomass into crude bio-oil that can be further upgraded into transportation fuel. Generally, fast pyrolysis is conducted at high temperatures (∼450–700 ℃) with high heating rate (∼10–100 ℃min −1) and short residence time (<5 mins) . During fast pyrolysis, lignocellulosic components within the
Mar 15, 2016 · The fast pyrolysis behaviour of pretreated banagrass was examined at four temperatures (between 400 and 600 C) and four residence times (between ~1.2 and 12 s). The pretreatment used water washing/leaching to reduce the inhaiqi content of the banagrass. Yields of bio-oil, permanent gahaiqi and char were determined at each reaction condition and compared to previously published results from
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Aug 30, 2019 · The pyrolysis behavior, kinetics and thermodynamics analysis of Napier grass were studied. A thermogravimetric analyzer (TGA) and differential thermal analyzer (DTA), at four heating rates: 5, 10, 20 and 30 o C/min were used in the experiments. Pyrolysis parameters were determined using model-fitting with the Coat-Rhaiqiern method.
Generally, pyrolysis process is classified into slow, 80 intermediate and fast pyrolysis. In slow pyrolysis (carbonization), temperature up to 400 °C, 81 vapor residence time of 60 minutes to days are used and a typical product yield of about 35 % bio-char, 3082 % bio-oil, and 35 % non-condensable gas. For fast pyrolysis, temperature of about
Apr 08, 2017 · This study presents in-situ upgrading of pyrolysis vapour derived from Napier grass over microporous and mesoporous ZSM-5 catalysts. It evaluates effect of process variables such catalyst–biomass ratio and catalyst type in a vertical fixed bed pyrolysis system at 600 °C, 50 °C/min under 5 L/min nitrogen flow. Increasing catalyst–biomass ratio during the catalytic process with microporous
Rising global demand for biodegradable mahaiqials and green sources of energy has brought attention to lignin. Herein, we report a method for manufacturing standalone lignin membranes without additives for the first time to date. We demonstrate a scalable method for macroporous (∼100 to 200 nm pores) lignin membrane production using four different organosolv lignin mahaiqials under a humid
Biomass has played an increasingly important role in the consumption of energy worldwide because of its renewability and carbon-neutral property. In this work, the pyrolysis mechanism of wheat straw is explored using reactive force field molecular dynamics simulations. A large-scale wheat straw model composed of cellulose, hemicellulose, and lignin is built. After model validation, the
A novel hybrid of pearl millet and napier grass (Pennisetum glaucum [L.] R. Br. x Pennisetum purpureum Schumach), PMN10TX15, was charachaiqized and investigated as an alternative energy source. Pyrolysis reactions of the PMN10TX15 were carried out in a batch reactor operated at 400-600 °C and haiqipheric pressure, aiming to investigate its
Fast pyrolysis of waste mahaiqials Pyrolysis liquid yield and quality is dependent on the feedstock. Highest liquid yield is obtained with bark free wood and lowest with agro-biomass. Ash content correlates to liquid yield Alkali metals, mainly potassium are known to catalyse pyrolysis reactions to yield more gas and water and
Nov 01, 2018 · Based on the above limitations, this article propohaiqi a system for the production of pyrolysis oil by using Napier grass with the feeding rate between 45 to 75 kg per hour. A Circulating Fluidized Bed reactor (CFBr) has been employed in this work because it offers more advantages than other reactors (Bridgwater, 2003). Liquid Petroleum Gas (LPG) and NCG were used as the fuels to produce heat into the reactor, and a cross flow heat exchanger was used to recover heat and to return it back into
Fast pyrolysis from Napier grass for pyrolysis oil production by using circulating Fluidized Bed Reactor: Improvement of pyrolysis system and production cost Energy Reports 10.1016/j.egyr.2018.08.004
Jun 02, 2020 · Fast pyrolysis from Napier grass for pyrolysis oil production by using circulating fluidized bed reactor: Improvement of pyrolysis system and production cost. Energy Reports 4: 565-575. Khezri R., Azlina W. and Tan H.B., 2016.