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Charcoal preparation method and special charcoal preparation drying device during carbon disulfide production

A carbon disulfide and drying device technology, applied in drying, drying machine, heating device and other directions, can solve the problems of reducing production efficiency, hindering the normal progress of the reaction, incomplete moisture drying, etc., and achieving the effect of reducing the consumption of raw materials

Inactive Publication Date: 2016-02-10
濮阳天泓实业有限公司
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0008] In order to ensure that the amount of carbon prepared meets the needs and efficiency of production, the inner chamber of the combustion furnace is generally larger. Black carbon or semi-coke in the inner chamber of the vertical barrel-shaped combustion furnace will often be heated unevenly due to uneven ventilation, and the ventilation is good. The charcoal preparation has been overheated, semi-coke is brittle, and a large amount of invalid powder is produced, resulting in increased loss. The ineffective powder entering the reactor will also hinder the normal progress of the reaction and increase the amount of slag, reducing production efficiency; If it is relatively low, there will be a phenomenon of semi-burnt and not red, and it will not be able to participate in the reaction normally. In severe cases, the drying of water will not be complete, and hydrogen sulfide gas will be produced when it enters the reaction. Therefore, in order to ensure sufficient heating, over-burning is often used in production. To ensure that the heat standard and drying standard are met
The consumption of carbon raw materials is very large, especially in the process of burning carbon raw materials themselves, a large amount of carbon is discharged in the form of carbon dioxide after combustion, which not only causes waste, but also causes air pollution

Method used

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  • Charcoal preparation method and special charcoal preparation drying device during carbon disulfide production
  • Charcoal preparation method and special charcoal preparation drying device during carbon disulfide production
  • Charcoal preparation method and special charcoal preparation drying device during carbon disulfide production

Examples

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Effect test

Embodiment 1

[0025] Embodiment 1: refer to figure 1 , is a schematic structural view of the carbon preparation drying device used in Example 1 of the present invention, including a drying chamber 18 composed of a housing 13, the drying chamber 18 is provided with a feed inlet 16, a dry air outlet 17, and a dry air inlet A14 , discharge port 11 and discharge door 12, a heating interlayer 10 is provided on the periphery of the housing 13 that constitutes the drying chamber 18, and the heating interlayer 10 is provided with a heat medium inlet 19 and a heat medium outlet 15, the central position of the drying chamber A central drying air intake mechanism is provided, and the central drying air intake mechanism includes a vertical distributor 31 and a dry air inlet B (33). The distributor 31 is a vertical pipe body, and the pipe body wall is provided with Uniformly distributed gas outlet 32, the gas outlet 32 ​​is from the inside of the distributor 31 pipe body to the outside of the pipe body ...

Embodiment 2

[0029] Embodiment 2: refer to figure 2 , is a schematic structural diagram of the carbon preparation drying device used in Embodiment 2 of the present invention. Compared with Embodiment 1, the difference of this embodiment is that the distributor 31 of the drying air intake mechanism in the drying chamber consists of multiple parallel Vertical pipe body composition.

Embodiment 3

[0030] Embodiment 3: refer to image 3 , is a schematic structural diagram of the carbon preparation drying device used in Example 3 of the present invention. Compared with the previous embodiments, the difference of this embodiment is that the dry air inlet A14 extends into the drying chamber 18 and the front end The air outlet is curved downward. Certainly, the air outlet 32 ​​of the distributor 31 may also have the same or similar structure.

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Abstract

The invention discloses a charcoal preparation method and a special charcoal preparation drying device during carbon disulfide production. The charcoal preparation method and the special charcoal preparation drying device during carbon disulfide production are characterized in that black charcoal or semi-coke serves as raw materials, and the raw materials are dried at the temperature of 350-450 DEG C; the charcoal preparation drying device comprises a drying chamber (18) composed of a shell (13); a heating interlayer (10) is arranged on the periphery of the shell (13); a central drying air inlet mechanism is arranged in the center of the drying chamber. Compared with the prior art, the raw material consumption can be greatly reduced, and especially energy saving and environmental friendliness are further achieved.

Description

technical field [0001] The invention belongs to the technical field of carbon disulfide production, in particular to a method for preparing carbon during production of carbon disulfide and a special drying device for preparing carbon. Background technique [0002] At present, the methods for producing carbon disulfide mainly include charcoal sulfur method, semi-coke batch production method and natural gas method. [0003] The charcoal sulfur method has been eliminated by the state because it uses a lot of wood to burn charcoal and destroys forest resources. [0004] Due to the large one-time investment, high production cost, and the natural gas source, the natural gas method is currently only available in a few areas. [0005] The semi-coke production method mainly uses black carbon or semi-coke as the carbon raw material. This method has rich raw material resources, relatively simple equipment, and low investment. Therefore, the production cost is low and the product quali...

Claims

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Application Information

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IPC IPC(8): F26B9/06F26B21/00F26B23/10F26B25/00
CPCF26B9/06F26B21/001F26B23/10F26B25/00
Inventor 张贯彪
Owner 濮阳天泓实业有限公司
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