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Segmented water removing and drying system for high-humidity coal and application method for segmented water removing and drying system

A drying system and high-humidity technology, applied in the direction of drying machine combination, drying solid materials, heating to dry solid materials, etc., can solve the problems of high energy consumption and changing the physical characteristics of filter cakes, so as to save energy consumption and increase the temperature of raw coal , to avoid the effect of energy consumption

Active Publication Date: 2015-12-16
SHANDONG UNIV
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  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

The patent with application number CN201210221818.7 uses microwave drying to dry the filter cake with a moisture content of 30%. However, the moisture is removed in gaseous form, which obviously consumes a lot of energy, and the filter cake will be broken and changed during the dehydration process. some physical properties of the filter cake
In addition, the patent application number CN200910259256.3 uses microwaves to heat and dehydrate pre-dried coal, and uses the waste heat of drying to perform hot pressing or thermoplastic molding. However, this patent mainly emphasizes hot pressing or thermoplastic molding processes and waste heat At the same time, the moisture in coal is also removed in gaseous form, which consumes a lot of energy

Method used

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  • Segmented water removing and drying system for high-humidity coal and application method for segmented water removing and drying system
  • Segmented water removing and drying system for high-humidity coal and application method for segmented water removing and drying system

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Embodiment 1

[0042] figure 1 It is a structural diagram of the segmental dehydration drying system in the present invention, the system includes a blanking mechanism for blanking (raw coal, particle size between 30-100mm) and preheating, and the blanking mechanism is a vertically arranged raw coal bunker 1. A heat exchange pipe is arranged along the inner wall of the raw coal bunker 1, and a condensate collection tank 11 is arranged at the bottom of the raw coal bunker 1, and the inlet end of the heat exchange pipe is connected to the outlet end of the dehumidification pump 8. A first microwave drying mechanism 2 is horizontally provided below the raw coal bunker 1, and a horizontally arranged first transmission mechanism 3 for transferring raw coal to the entrance of the solid-liquid separation mechanism 5 is arranged inside the first microwave drying mechanism 2 for solid-liquid separation. The mechanism 5 is arranged vertically or obliquely, the end of the first conveying mechanism 3 is...

Embodiment 2

[0066] The segmental dehydration drying system includes a blanking mechanism 1, a first microwave drying mechanism 2, a first transmission mechanism 3, a solid-liquid separation mechanism, a second microwave drying mechanism 6 and a third transmission mechanism 7, wherein the first microwave drying mechanism 2, The structures of the first conveying mechanism 3, the third conveying mechanism 7 and the second microwave drying mechanism 2 are the same as those in Embodiment 1, and the solid-liquid separation mechanism is the fourth conveying mechanism 14 arranged obliquely, and the fourth conveying mechanism 14 includes two Two rollers, a mesh conveyor belt is set between the two rollers, and a vibrating motor fixed to the conveyor belt is arranged under the upper conveyor belt. When the coal material falls from the first conveying mechanism 3 to the fourth conveying mechanism 14, the fourth conveying mechanism The conveying mechanism 14 transports the coal material to the third c...

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Abstract

The invention discloses a segmented water removing and drying system for high-humidity coal and an application method for the segmented water removing and drying system. The system comprises a discharging mechanism. A first microwave drying mechanism is arranged below the discharging mechanism and internally provided with a first conveying mechanism. A solid-liquid separation mechanism is arranged at the tail end of the first conveying mechanism. A second conveying mechanism is arranged at an outlet of the solid-liquid separation mechanism. A second microwave drying mechanism is arranged at the tail end of the second conveying mechanism. The segmented water removing and drying system has the beneficial effects that a microwave heating manner and a non-heating manner are combined with the water removing and drying technology, a heat water removing manner and a non-heat water removing manner are organically combined, water in coal is removed in the form of a liquid state on the basis of low-rank coal microwave drying, and energy consumption of a microwave drying system is greatly reduced; raw coal is heated through the reutilization of residual heat and waste heat generated by the drying system, and the economical efficiency of the whole drying system is improved; and after deep drying is carried out, utilization of later finished coal is more flexible and safer, and the processing cost is reduced.

Description

technical field [0001] The invention relates to coal drying, in particular to a segmental dehydration drying system for high-humidity coal and its application method. Background technique [0002] In recent years, from the perspective of my country's primary energy consumption structure and trends, although the proportion of low-rank coal in my country's primary energy consumption has declined, its production and consumption continue to increase, and the shortage of high-rank coal resources has gradually become a problem that my country must face. outstanding issues. The low-rank coal reserves in my country account for 40% of the total coal reserves, of which lignite accounts for about 12.8% of the total coal reserves in my country. Low-rank coal is playing an increasingly important role in the energy supply process. [0003] High-moisture coal mainly refers to (low-rank coal with high moisture content (30%-65%)) which is not conducive to long-distance transportation and sto...

Claims

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Application Information

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IPC IPC(8): F26B20/00F26B7/00F26B3/347F26B5/08
Inventor 宋占龙赵希强朱俊志姚连升井传明王文龙毛岩鹏马春元陈磊
Owner SHANDONG UNIV
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