Eureka AIR delivers breakthrough ideas for toughest innovation challenges, trusted by R&D personnel around the world.

A biomass pyrolysis co-production gas/biochar production process

A biomass pyrolysis and biomass gas technology, which is applied in the fields of biofuels, petroleum industry, indirect heating and dry distillation, etc., can solve the problems of unstable gasification, poor economic benefits, low calorific value, etc., and achieve simple and reliable production equipment. Advanced technology and good production efficiency

Active Publication Date: 2018-08-03
HEFEI DEBO BIOENERGY SCI & TECH
View PDF5 Cites 1 Cited by
  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

my country is rich in biomass fuel resources. The total amount of biomass resources that can be used as energy in the country is about 460 million tons of standard coal per year, but currently only 22 million tons of standard coal are used, and the utilization rate is less than 5%. Most of them still use incineration, Landfill and other means to deal with serious pollution
However, many links such as biomass collection and transportation in my country are relatively extensive, and the characteristics of biomass itself cause the available biomass to have the characteristics of high moisture, low calorific value, and high alkalinity. The degasification process leads to low carbon production rate and poor economic benefits, and when the biomass raw material has high moisture content, the gasification is unstable

Method used

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
View more

Image

Smart Image Click on the blue labels to locate them in the text.
Viewing Examples
Smart Image
  • A biomass pyrolysis co-production gas/biochar production process

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0027] 25% water content, 3 cm particle diameter wood blocks are fed into the pyrolysis gasification auger 2 through the feeding device 3 . The pyrolysis and gasification auger 2 continuously transports the biomass. After heating, the free water and bound water in the biomass evaporate, and the temperature is measured after passing through the temperature monitor 203 (T1 is 80°C, T2 is 120°C, and T3 is 140°C) Selectively open the regulating valve 202 (T2 post-regulating valve), and discharge the steam through the steam induced draft fan 201 . The biomass raw material continues to be transported through the pyrolysis and gasification auger 2 for pyrolysis and gasification to generate high-temperature biomass gas and biochar. In the pyrolysis gasification auger 2, the raw material is separated by high-temperature biomass gas and biochar through the charcoal gas separation device 4, and the separated biochar is collected. The fixed carbon content of the biochar is 80.7%; the spec...

Embodiment 2

[0029] The rice husks with a water content of 15% and a particle diameter of 2 cm are fed into the pyrolysis and gasification auger 2 through a feeding device 3 . The pyrolysis and gasification auger 2 continuously transports the biomass. After heating, the free water and bound water in the biomass evaporate, and the temperature is measured after passing through the temperature monitor 203 (T1 is 110°C, T2 is 140°C, and T3 is 160°C) Selectively open the regulating valve 202 (open the regulating valve after T1), and discharge the steam through the steam induced draft fan 201. The biomass raw material continues to be transported through the pyrolysis and gasification auger 2 for pyrolysis and gasification to generate high-temperature biomass gas and biochar. In the pyrolysis gasification auger 2, the raw material is separated by high-temperature biomass gas and biochar through the charcoal gas separation device 4, and the separated biochar is collected. The fixed carbon content ...

Embodiment 3

[0031] 33% water content, 8 cm particle size bamboo pieces are fed into the pyrolysis and gasification auger 2 through the feeding device 3 . The pyrolysis and gasification auger 2 continuously transports the biomass. After heating, the free water and bound water in the biomass evaporate, and the temperature is measured after passing through the temperature monitor 203 (T1 is 60°C, T2 is 102°C, and T3 is 120°C) Selectively open the regulating valve 202 (the regulating valve after opening T3), and discharge the steam through the steam induced draft fan 201. The biomass raw material continues to be transported through the pyrolysis and gasification auger 2 for pyrolysis and gasification to generate high-temperature biomass gas and biochar. In the pyrolysis gasification auger 2, the raw material is separated by high-temperature biomass gas and biochar through the charcoal gas separation device 4, and the separated biochar is collected. The fixed carbon content of the biochar is 8...

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
Login to View More

PUM

PropertyMeasurementUnit
sizeaaaaaaaaaa
particle diameteraaaaaaaaaa
diameteraaaaaaaaaa
Login to View More

Abstract

The invention discloses a biomass pyrolysis gas / charcoal co-production device and process. The co-production device comprises a fluidized bed gas burner, a pyrolysis gasification auger, a vapor discharge system, a charging device, a gas-charcoal separation device, a high-temperature gas booster fan, an air preheater and other equipment. The production process comprises the steps that biomass materials are conveyed into the pyrolysis gasification auger for pyrolysis and gasification reaction; in the reaction process, water vapor generated at the drying layer is discharged through the vapor discharge system, charcoal generated after pyrolysis and gasification and high-temperature biomass gas with a low heating value are separated through the separation device to obtain high-quality charcoal, and a part of the generated high-temperature biomass gas with the low heating value is output into the fluidized bed gas burner for reaction; meanwhile, bed materials are fluidified to supply heat to the pyrolysis gasification auger so as to keep the pyrolysis and gasification reaction continuous. By the adoption of the process, the method is advanced, production equipment is simple and reliable, the yield rate of charcoal from biomass is high, and the production effect is good.

Description

technical field [0001] The invention belongs to the technical field of biomass utilization, and in particular relates to a biomass pyrolysis co-production gas / biochar production process. Background technique [0002] With the increasingly prominent global energy and environmental issues, the development of new energy sources has become an urgent task. As a clean energy source, biomass has a net carbon dioxide emission to the atmosphere that is close to zero. The content of nitrogen and sulfur in biomass is extremely low, and the emissions of nitrogen oxides and sulfides are very low during energy conversion. Vigorously developing biomass fuel resources will help improve my country's energy structure dominated by fossil fuels and reduce emissions of sulfides and nitrogen oxides. This will not only alleviate the greenhouse effect, but also reduce the content of carbon dioxide in the atmosphere. my country is rich in biomass fuel resources. The total amount of biomass resourc...

Claims

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
Login to View More

Application Information

Patent Timeline
no application Login to View More
Patent Type & Authority Patents(China)
IPC IPC(8): C10B53/02C10B47/20C10B47/44
CPCY02E50/10Y02P20/129
Inventor 张齐生张守军周建斌赵成武鲁万宝张守峰冯干吴银龙李益瑞胡鹏
Owner HEFEI DEBO BIOENERGY SCI & TECH
Who we serve
  • R&D Engineer
  • R&D Manager
  • IP Professional
Why Eureka
  • Industry Leading Data Capabilities
  • Powerful AI technology
  • Patent DNA Extraction
Social media
Eureka Blog
Learn More
PatSnap group products