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Drying furnace or pyrolyzing furnace with rotary beds

A technology of rotating material bed and pyrolysis furnace, which is applied to furnaces, coke ovens, furnace types, etc., can solve the problems of back-mixing and tandem of materials, deterioration of heat transfer uniformity, and deterioration of uniformity of pyrolysis.

Active Publication Date: 2013-11-13
CHNA ENERGY INVESTMENT CORP LTD +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Since the movement of the material on the material bed is only pushed and guided by the guide rake 28, and there is no physical barrier between different material rows, the controllability of the material movement is relatively weak
During the rotation process, the materials located in different rows are prone to back-mixing and cascading, etc., which makes the thickness and residence time of the materials on the rotating material bed different, and the uniformity of heat transfer and the degree of uniformity of pyrolysis also deteriorate.
When the above-mentioned rotary hearth furnace is enlarged to an industrial application scale, the situation of back-mixing and cascading of materials between different columns is more serious, so that the quality, stability, and economical efficiency of coal pyrolysis are adversely affected

Method used

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  • Drying furnace or pyrolyzing furnace with rotary beds
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  • Drying furnace or pyrolyzing furnace with rotary beds

Examples

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Embodiment approach

[0034] As an exemplary embodiment of the present invention, the closed case 10 may include an upper case 102 with a conical top and a lower case 104 connected to the upper case 102, wherein the upper case 102 and the lower case 104 A water seal is provided between them, and the pressure in the housing 10 can be maintained at atmospheric pressure or slightly positive pressure. The inner space formed by the upper casing 102 and the lower casing 104 accommodates N rotating material beds 30, and the central rotating shaft (discharging pipe) 40 is arranged along the center line of the casing 10, and extends downward through the lower casing 104 and bearings. (not shown) and transmission (not shown).

[0035] In one embodiment of the present invention, N rotating material beds 30 define N moving trajectories of materials. Each rotating material bed 30 includes a rotatable annular planar bed bottom 301 and an inner wall 302 and an outer wall 303 that are stationary relative to the b...

Embodiment 1

[0061] use Figure 1-Figure 5 The shown drying furnace or pyrolysis furnace of the present invention carries out low-temperature pyrolysis of Hulunbeier lignite in the following Table 1 and Table 2 for its industrial analysis and elemental analysis respectively. The benchmarks for industrial analysis and elemental analysis are both air-dry bases, while elemental analysis is only for organic matter, excluding ash and moisture.

[0062] Table 1

[0063]

[0064] Table 2

[0065]

[0066] The Hulunbeier lignite with a particle size of 15-50 mm obtained through crushing and screening is continuously sent into the above-mentioned drying furnace or pyrolysis furnace 100 on an industrial scale, and a furnace with an oxygen content of 0.8% and a temperature of 700 ° C is introduced into it. Oxygen-deficient hot gas is subjected to low-temperature pyrolysis with the following process parameters and operating conditions.

[0067] The structural parameters of the pyrolysis furna...

Embodiment 2

[0080] The Hulunbeier lignite with a particle size of 15-30 mm obtained through crushing and screening is continuously sent into the above-mentioned drying furnace or pyrolysis furnace 100 on an industrial scale, and an anaerobic furnace with an oxygen content of 0.8% and a temperature of 850 °C is passed through. The hot gas is subjected to low-temperature pyrolysis with the following process parameters and operating conditions.

[0081] The structural parameters of the pyrolysis furnace 100:

[0082] Daily processing capacity: 5000 tons / day;

[0083] Feed density 705kg / m 3 ;

[0084] The overall height of the rotating material bed: 2.5m, the minimum inner diameter: 5m,

[0085] The outer diameter of the pyrolysis furnace: 20m;

[0086] The pyrolysis furnace includes 5 gradually rising rotating material beds, the width of which is: W 1 = 2.5m, W 2 =1.6m, W 3 =1.3m; W 4 =1.1m, W 5 =0.99m;

[0087] The material flow thickness in the rotating material bed is 500mm.

...

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Abstract

The invention discloses a drying furnace or pyrolyzing furnace with rotary beds. The drying furnace or the pyrolyzing furnace comprises a closed shell, N concentric ring planar rotary beds, a feed port, N stop plates, N discharge ports and at least one pyrolysis gas product outlet and / or one tail gas outlet, wherein the N concentric ring planar rotary beds are positioned in the shell; the two ends of the stop plates are seamlessly connected with the inner walls and the outer walls of the corresponding rotary beds respectively; each rotary bed comprises a rotatable planar bed bottom and an inner wall and an outer wall which are kept still relative to the bed bottom; the bed bottom of each rotary bed is provided with at least one through hole; and the heights of the N rotary beds rise gradually from inside to outside and seamless connection is realized. When a material is rotated to the position of a stop plate along with the bed bottom of a rotary bed, the material is pushed from outside to inside by the stop plate so as to fall into the next joined rotary bed through a discharge port; and thus, the material falls from outside to inside step by step, is conveyed to the position of the discharge port of the innermost rotary bed through the bed bottoms of the N rotary beds and is finally discharged out of the drying furnace or the pyrolyzing furnace through the discharge port.

Description

technical field [0001] The invention relates to a drying furnace or a pyrolysis furnace with a rotating material bed, in particular to a drying furnace or a pyrolysis furnace with a rotating material bed for solid carbonaceous materials. Background technique [0002] In the context of the increasing shortage of global oil and gas resources, how to rationally utilize coal resources in a low-cost and environmentally friendly manner to realize coal's supplementation and even substitution of oil and gas resources has become an important research topic in the energy industry. [0003] After many years of research and a large number of experiments, it can be determined that the rational utilization of coal resources is to refine and comprehensively utilize coal according to the different characteristics of coal quality and coal types. Drying and pyrolysis technology is one of the basic ways for coal graded refining and comprehensive utilization. Generally, the pyrolysis of solid ...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): F27B9/16C10B49/06
Inventor 卢洪崔哲陈微闵健翁力刘科
Owner CHNA ENERGY INVESTMENT CORP LTD
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