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Hydrogasification semi-coke pulping apparatus and stable operation method thereof

A hydrogenation gasification and stable operation technology, applied in the field of coal chemical industry, can solve the problems of blockage and damage of the filter 28 and induced draft fan 27, reduce the gasification efficiency of coal-water slurry, affect the gasification process of coal-water slurry, etc., and achieve improvement Pulping effect, improving the utilization rate of semi-coke, and ensuring the effect of continuous and stable operation

Pending Publication Date: 2019-10-22
XINNENG ENERGY CO LTD
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Due to the loose and porous semi-coke texture, when it is mixed with water, it often floats on the water surface and is difficult to mix. The pulping effect is poor, and about 10% of the semi-coke by mass ratio cannot be successfully pulped. In order to ensure the pulping quality, this part is not used. The semi-coke mixed with water is generally drawn out of the pulping mixing tank 1 through the filter 28 and the induced draft fan 27. In this process, on the one hand, about 10% of the semi-coke is not effectively utilized, resulting in a waste of resources. The atmospheric environment has certain pollution; on the other hand, the filter 28 and the induced draft fan 27 are in contact with the semi-coke for a long time, and the filter 28 and the induced draft fan 27 are prone to blockage and damage, which affects the continuous and stable pulping process. Interruption will affect the progress of the coal-water slurry gasification process and reduce the efficiency of coal-water slurry gasification

Method used

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  • Hydrogasification semi-coke pulping apparatus and stable operation method thereof
  • Hydrogasification semi-coke pulping apparatus and stable operation method thereof
  • Hydrogasification semi-coke pulping apparatus and stable operation method thereof

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0024] like Figure 2-3 As shown, the hydrogasification semi-coke pulping device includes a pulping stirring tank 1, a Venturi mixer 2 is provided at the feeding port of the pulping stirring tank 1, and a pulping agitator is arranged in the pulping stirring tank 1 3. The top of the rotating shaft of the pulping agitator 3 passes through the top of the pulping stirring tank 1 and is fixedly connected with the output shaft of the pulping rotating motor 4. The top of the pulping stirring tank 1 is provided with a semi-coke processing chamber 5, which The inside of 5 communicates with the inside of the pulping stirring tank 1, the bottom of the semi-coke processing chamber 5 is connected with the top of the pulping stirring tank 1, and the top of the semi-coke processing chamber 5 is provided with an emptying pipe 6; There are at least two trays 7 in the shape of a superior arc in a staggered manner. In this embodiment, the number of trays 7 is 4, and the trays 7 are arranged hori...

Embodiment 2

[0027] Using the stable operation method of the hydrogasification semi-coke pulping device carried out in Example 1, the semi-coke is pneumatically transported into the Venturi mixer 2 and mixed with the industrial fresh water transported into the Venturi mixer 2, and the pressure of the pneumatic transport is The operating pressure of pulping stirring tank 1 is 0.1MPa, the mixing mass ratio of semi-coke and industrial fresh water of Venturi mixer 2 is 1:0.8, and the outlet of Venturi mixer 2 is placed in pulping stirring tank 1 Below the inner liquid level, the pre-pulp is obtained after mixing; the pre-pulp enters the slurry mixing tank 1 for stirring, and the stirring speed is 30r / min; during the stirring process, the industrial fresh water is passed into the semi-coke processing chamber 5 , the mixed mass ratio of the pneumatically conveyed semi-coke and the industrial fresh water passing into the semi-coke treatment chamber 5 is 1:0.8, and the industrial fresh water flows ...

Embodiment 3

[0033] Using the stable operation method of the hydrogasification semi-coke pulping device carried out in Example 1, the semi-coke is pneumatically transported into the Venturi mixer 2 and mixed with the industrial fresh water transported into the Venturi mixer 2, and the pressure of the pneumatic transport is The operating pressure of pulping stirring tank 1 is 0.15MPa, the mixing mass ratio of semi-coke and industrial fresh water of Venturi mixer 2 is 1:0.9, and the outlet of Venturi mixer 2 is placed in pulping stirring tank 1 Below the inner liquid level, pre-pulp is obtained after mixing; the pre-pulp enters the pulping mixing tank 1 for stirring, and the stirring speed is 40r / min; during the stirring process, pass industrial fresh water into the semi-coke processing chamber 5 , the industrial fresh water flows along the upper surface of the tray 7, forming a layer of water film on the upper surface of the tray 7, part of the semi-coke that has not been mixed with the indu...

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Abstract

The invention discloses a hydrogasification semi-coke pulping apparatus and a stable operation method thereof. The apparatus comprises a pulping stirring tank, a pneumatic conveying device, a venturimixer and a pulp blending tank. The stable operation method comprises that semi-coke is pneumatically conveyed into a venturi mixer, and is mixed with industrial fresh water conveyed to the venturi mixer to obtain a pre-pulp. According to the present invention, semi-coke is conveyed to the venturi mixer through pneumatic conveying, and is mixed with the industrial fresh water, the semi-coke is fully wetted in advance, the wet semi-coke is conveyed to the pulping stirring tank, and the semi-coke directly enters the liquid surface of the pulping stirring tank, and is subjected to stirring pulping with the industrial fresh water in the pulping stirring tank, such that the semi-coke is mixed into the industrial fresh water to the maximal degree so as to improve the utilization rate of the semi-coke and improve the pulping effect.

Description

Technical field: [0001] The invention relates to the field of coal chemical industry, in particular to a hydrogasification semi-coke pulping device and a stable operation method thereof. Background technique: [0002] Hydrogasification refers to the process in which carbon-containing compounds react with hydrogen at medium temperature (700-1000°C) and high pressure (5-10MPa) to generate crude gas rich in methane, high value-added aromatic oil and semi-coke with high calorific value . Semi-coke, also known as low-temperature coke, is gray-black, with higher volatiles than coke, loose and porous texture, and good reactivity. It is often used as a raw material for coal-water slurry gasification in the field of coal chemical industry. [0003] At present, the process of using semi-coke for coal-water slurry gasification is roughly as follows: figure 1 As shown, the semi-coke is ground by the semi-coke mill 19, and the semi-coke with a qualified particle size is ground into the...

Claims

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Application Information

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IPC IPC(8): B01F13/10B01F7/18C10B55/00C10L3/08
CPCC10B55/00C10L3/08B01F27/90B01F33/811
Inventor 冯浩李美喜李维张刚王凤彬王银明
Owner XINNENG ENERGY CO LTD
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