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High-moisture sludge pyrolysis method and device

A pyrolysis and sludge technology, which is applied in the pyrolysis treatment of sludge, gasification process, petroleum industry, etc., can solve the problems of small heating and heat transfer area, large energy consumption, low utilization rate, etc. Increase the response time, the effect of large processing capacity

Active Publication Date: 2017-02-22
NANJING UNIV OF TECH
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

However, the drying and gasification cracking processes are still carried out separately, resulting in more equipment in the whole system, complex structure, low overall efficiency and high cost. In addition, the distribution of water vapor entering the gasification cracking furnace is not uniform enough, and the use of low rate
Chinese patent document CN205045973U provides a new type of sludge pyrolysis device, which belongs to the screw propulsion type and has a relatively simple structure. Too large, not suitable for process production; external heating has a small heat transfer area, low heat and mass transfer efficiency, and almost no reaction space

Method used

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  • High-moisture sludge pyrolysis method and device

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Experimental program
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Effect test

Embodiment 1

[0036] combine Figure 1~5 The present invention is further described.

[0037] A pyrolysis device for high-humidity sludge, consisting of a hollow shaft 1, a casing 2, a scraper 3, a set of hollow discs 4, a heat medium drainage pipe 5, an expansion joint 6, a propeller 7, and a heat medium delivery pipe 8 , agitator 9, sliding support 10, sealed feed system 11, sealed discharge system 12, biomass powder burner 13, material inlet A, material outlet B and gas outlet C; wherein the hollow shaft 1 is close to the biomass powder combustion One end of device 13 is connected to heat medium inlet G 1 , the other end is connected to heat medium outlet G 2 , where shell 2 is close to heat medium outlet G 2 There is a material inlet A on the upper part of one end, which is connected to the sealed feeding system 11, and the shell 2 is close to the heat medium inlet G 1 There is a gas outlet C on the upper part of one end, and a material outlet B on the lower part, which is connected...

Embodiment 2

[0040] The main parameters of the high-humidity sludge pyrolysis device provided in this embodiment are as follows: the number of disks is 40, and the diameter of the disks is 120 cm; the distance between the two disks near the material inlet end is 17 cm, and the distance between the two disks near the material outlet end The distance between the two disks is 13cm; 6 agitators are arranged on the wall of each disk; the number of scrapers is 15, the height is 40cm, and the thickness is 5cm.

[0041] High-humidity sludge with a moisture content of 79.51% and biomass with a moisture content of 12.87% were used as pyrolysis raw materials in a ratio of 6:4. Among them, the sludge is taken from the dewatered sludge of a domestic sewage treatment plant in Nanjing, and the biomass micropowder comes from a wood processing plant in Wuhan. After the mixture is stirred evenly, the material inlet A continuously enters the disk device through the sealed feeding system. At this time, the hi...

Embodiment 3

[0047] The main parameters of the high-humidity sludge pyrolysis device provided in this embodiment are as follows: the number of disks is 20, and the diameter of the disks is 60 cm; the distance between the two disks near the material inlet end is 15 cm, and the distance between the two disks near the material outlet end The distance between the two disks is 10cm; 4 agitators are arranged on the wall of each disk; the number of scrapers is 5, the height is 15cm, and the thickness is 3cm.

[0048] Mixed material parameters are the same as in Example 2. After the mixture is stirred evenly, the material feed A continuously enters the disc device through the sealed feed system. At this time, the high-temperature flue gas enters G 1 The temperature at the place is about 1000℃, the flue gas flow rate is 8m / s, and the flue gas outlet G 2 The temperature at the place is about 150°C, and the flow velocity is 2m / s. The material entering the device is heated by the disc, shell and hol...

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Abstract

The invention relates to a high-moisture sludge pyrolysis method and device. The device is composed of a hollow shaft (1), a shell (2), a sludge scraper (3), a set of hollow disks (4), a heat medium drainage pipe (5), an expansion joint (6), a propeller (7), a heat medium delivery pipe (8), a stirrer (9), a slide support (10), a sealed feed system (11), a sealed discharge system (12), a biomass micropowder combustor (13), a material inlet (A), a material outlet (B) and a combustible gas outlet (C). The high-temperature flue gas stably flows into the disks through the drainage pipe on the heat medium delivery pipe to perform heat conduction on the disks, so that the material is indirectly heated by the disks, shell and hollow shaft so as to be pyrolyzed. The method and device have the characteristics of high treatment capacity, stable operation, simple process, no secondary pollution, high recyclability and the like, and are economical and environment-friendly. The method and device can implement pyrolysis on high-moisture sludge, food residues, decoction dregs, wine stillage, resins and other organic wastes, thereby achieving the goals of waste treatment and recycling.

Description

technical field [0001] The invention relates to a pyrolysis method and device for high-humidity sludge, which belongs to the field of engineering thermophysics and environmental science and technology, and can be used to treat sludge (municipal, chemical, petroleum, papermaking, paint, etc.), food residues, pharmaceuticals, etc. Slag, wine residue, resin, etc., use high-temperature pyrolysis to achieve efficient disposal and resource utilization. Background technique [0002] The water content of sludge is generally high, and the water content of ordinary sludge is as high as 80%. Even after being treated by digestion techniques such as dosing and filtration, the water content is still as high as 60%, which greatly affects its energy density and quality. At present, the more advanced thermochemical conversion method generally requires the water content to be reduced to below 20%, resulting in higher cost of drying treatment in the early stage, and the material needs water va...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C02F11/10C10J3/00
CPCC10J3/00C02F11/10C10J2300/0923C10J2300/092C10J2300/0976C10J2300/0909Y02W10/40
Inventor 朱跃钊朱锦娇杨丽陈海军万龙
Owner NANJING UNIV OF TECH
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