Looking for breakthrough ideas for innovation challenges? Try Patsnap Eureka!

A falling pyrolyzer

A pyrolyzer and pyrolysis technology, used in special forms of dry distillation, biofuels, coke ovens, etc., can solve the problems of inability to efficiently complete pyrolysis, unfavorable full pyrolysis of large particles, and short residence time. The ability to expand and contract is strong, it is not easy to raise dust, and the effect of improving the calorific value

Active Publication Date: 2016-08-24
TONGJI UNIV
View PDF13 Cites 0 Cited by
  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

The down-bed pyrolysis reactor can realize rapid pyrolysis of small particle solid fuel, and the residence time of pyrolysis gas is short, but the residence time is too short for solid fuel with large particle size, which is not conducive to the sufficient pyrolysis of large particles. Although the invention Utilize moving bed to solve this problem, but moving bed only handles large particles and is too inefficient
[0009] In view of the fact that the existing pyrolysis technology and reactors cannot meet the requirements of efficient pyrolysis, clean volatile matter, and simple post-treatment, the present invention proposes a highly efficient, economical, and stable-operating drop-down pyrolysis reactor, To ensure that waste and biomass can be pyrolyzed more economically, safely and efficiently, and the volatiles produced by pyrolysis are cleaner and will not carry a lot of dust

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 falling pyrolyzer
  • A falling pyrolyzer
  • A falling pyrolyzer

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0049] figure 1 It shows a specific optimized implementation of a descending pyrolyzer provided by the present invention. The pyrolyzer of this specific embodiment comprises a feeding port 1, a uniform feeding mechanism 2, and a water vapor outlet 3 in the preheating section; It is composed of a car frame connected by connecting pieces 18; the main reactor is composed of a vertical plate heat transfer surface 11; one side has a volatile matter filter layer 8 and its outlet 7; the other side has a heat source, that is, a heat source inlet for high-temperature flue gas 9 and heat source outlet 10; there is a heat source partition 13 between the inlet and outlet of the heat source; biomass and waste are discharged into the charcoal discharge section 14 after the main reactor is reacted; they are continuously discharged after a proper stay in the discharge section 14. The distance between the heat transfer surfaces 11 of the vertical plate (material side) is A, and the size is 1....

Embodiment 2

[0056] figure 2 It shows another specifically optimized implementation of the descending pyrolyzer provided by the present invention. The pyrolyzer of this specific embodiment comprises a feeding port 1, a uniform feeding mechanism 2, and a water vapor outlet 3 in the preheating section; It is composed of a car frame connected by connecting pieces 18; the main reactor is composed of a membrane-type vertical tube heat transfer surface 11; one side has a volatile matter filter layer 8 and its outlet 7; the other side has a heat source, that is, the inlet of high-temperature flue gas 9 and outlet 10; biomass and waste are discharged into the charcoal discharge section 14 after the main reactor reacts; they are continuously discharged after proper cooling in the charcoal discharge section 14. The distance between the heat transfer surfaces 11 of the film vertical tube is A; the diameter of the heat transfer surface is d; the length of the heat transfer surface is C; the width of...

Embodiment 3

[0060] After a certain sludge is dried, the moisture content is 30%, and the largest particle is below 28mm. Using the existing rotary pyrolysis reactor is easy to generate dust. A cyclone dust collector needs to be installed, and the cyclone dust collector is often blocked by tar. Adopt falling type pyrolyzer of the present invention ( figure 2 ), the sludge is fed to the preheating section by the uniform feeding mechanism 2; the generated water vapor is discharged from the water vapor outlet 3 of the preheating section, so that the moisture in the volatile matter is reduced and the calorific value is increased. The dry pre-reacted material then descends to the main reactor, which consists of vertical plates ( Figure 4) heat transfer surface 11, the distance B on the heat source side of the vertical plate is 15mm, high-temperature flue gas flows through, and the distance A on the sludge side is 45mm, heated to 600°C by the high-temperature flue gas, and the volatile matter...

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
Login to View More

Abstract

The invention relates to a falling-type pyrolyzer which comprises a feed opening, a uniform blanking mechanism, a preheating section, a main reactor, a blanking auxiliary mechanism and a charcoal discharge section from top to bottom. The waste or biomass, of which the size is less than 30mm and the water content is 35% or below, is sent into the preheating section by the uniform blanking mechanism, and sent to the main reactor by the preheating section. The preheating section is provided with a vapor outlet. The main reactor is composed of vertical plates or membrane-type vertical tube heat transfer surfaces, and the interval is 1.4-3 times of the maximum particle size; by the aid of the blanking auxiliary mechanism, one side is provided with a heat source port, and the other side is provided with a volatile matter filter layer perpendicular to the heat transfer surface and a discharge port. The generated coke falls into the charcoal discharge section, the unpyrolyzed material is pyrolyzed at the charcoal discharge section, and the retention time is controlled through the charcoal discharge speed. When cold charcoal needs to be discharged, the charcoal discharge section is converted into the cooling section, and a coolant passes through at the cold source side. The falling-type pyrolyzer can adapt to the thermal expansion and cold shrinkage, and has the advantages of no leakage, high capacity and space saving.

Description

technical field [0001] The invention belongs to the field of biomass utilization and waste resource treatment. In particular, the present invention relates to a descending pyrolyzer. Background technique [0002] At present, the types of reaction devices that can be used for sludge, biomass, and garbage pyrolysis mainly include fluidized bed pyrolysis reactors, fixed bed pyrolysis reactors, rotary pyrolysis reactors, moving bed pyrolysis reactors, Rotating cone reactors, down-tube pyrolysis reactors, etc., all have their own advantages in application, but they also have certain defects. [0003] Fluidized bed pyrolysis reactor and rotating cone reactor are more suitable for pyrolysis liquefaction and pyrolysis gasification of biomass particles, but not suitable for pyrolysis carbonization of biomass. Fixed bed pyrolysis reactor is more suitable for pyrolysis carbonization and pyrolysis gasification of biomass particles and waste, but not suitable for pyrolysis liquefaction...

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): C10B53/02C10B53/07C10B31/00C10B57/00
CPCY02E50/10Y02P20/143
Inventor 陈德珍窦晓敏戴晓虎赵云松
Owner TONGJI UNIV
Who we serve
  • R&D Engineer
  • R&D Manager
  • IP Professional
Why Patsnap Eureka
  • Industry Leading Data Capabilities
  • Powerful AI technology
  • Patent DNA Extraction
Social media
Patsnap Eureka Blog
Learn More
PatSnap group products