Composite pre-heater

A preheater and separator technology, applied in the directions of preheating cost, lighting and heating equipment, furnaces, etc., can solve the problems of low heat exchange efficiency, low preheating efficiency, large heat dissipation loss, etc., and achieve high heat exchange efficiency, The effect of long residence time and less heat loss

Inactive Publication Date: 2010-06-30
吕天宝 +1
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  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

However, the vertical preheater has great disadvantages in terms of thermal engineering: in the vertical preheater, the material and the air flow mainly conduct countercurrent heat exchange, and the material is both dispersed and aggregated in each bowl in the vertical cylinder, so Repeated circulation, satisfying heat exchange and countercurrent movement, because the separation efficiency of the vertical cylinder itself is low, it is generally installed in the upper part of the cyclone in series, and the thermal efficiency of the vertical cylinder preheater is much lower than that of the cyclone preheating due to poor material dispersion Therefore, in the international market, the vertical tube preheater was gradually eliminated
[0004] Most of the cyclone preheaters currently used in China have relatively low preheating efficiency, and the decomposition rate of calcium carbonate in the kiln material is only about 30%, which affects the kiln production capacity
In the five-stage cyclone preheater of the prior art, there is a columnar ascending flue between the tail smoke chamber of the cyclone cellar and the final cyclone tube. This structure leads to poor preheating effect of the cyclone preheater. The decomposition rate of materials entering the kiln cannot meet the requirements. Generally, the output of a five-stage cyclone preheater with a production capacity of 12.5t / h is only about 10t / h; the output of a kiln with a production capacity of 25t / h is only 21t / h around
Therefore, it not only affects the output of the kiln, but also increases the energy consumption.
This five-stage cyclone preheater technology has high plant building, high resistance, easy to clog and scarring, strict requirements on raw material alkali, chlorine and sulfur content, high investment and power consumption
[0005] The rotary dryer is a running equipment. When drying the material, the material is lifted by the internal lifting plate, forming a material curtain on the cross section of the dryer, and exchanging heat with the incoming hot air. The heat exchange efficiency is low, and it is easy to scar. Moreover, the diameter and length of the dryer are large, the investment is high, and the volume output is low
Because it is a running equipment, the air leakage is high, the heat dissipation loss is large, and the power consumption is high
[0006] They are not optimal in terms of resistance, energy consumption, efficiency, and investment

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0027] Example 1. Preheating cement raw meal

[0028] Manufacture of composite preheater: use ordinary steel plate to roll and weld the partial cone chamber 1, spray chamber 2, separator 4, spray chamber 2 and separator 4 connecting pipe, separator 4 discharge pipe. The partial cone chamber 1 is tapered on one side, and the upper part of the other side is cylindrical and the lower part is tapered. The height value is h 1 / h=0.5, there is an opening at the upper and lower ends, the inlet air speed is 8m / s, the outlet air speed is 9m / s, the cross-sectional wind speed is 4m / s; the eccentricity e is e / R 1 = 1.5, h 1 / h=0.5, h 2 / h=0.5, h / R 1 =3; The spray chamber 2 is a cylindrical hollow structure, the shell is made of steel plate welding, the inlet is frustum-shaped, the outlet is inverted frustum-shaped, the inlet and outlet air speed is 9m / s, the section wind speed is 6m / s, and the height value is h 2 / h=0.5. O 1 It is the center of the welding port of the partial cone chamber 1 a...

Embodiment 2

[0030] Example 2. Drying desulfurized gypsum

[0031] Manufacture of composite preheater: use ordinary steel plate to roll and weld the partial cone chamber 1, spray chamber 2, separator 4, spray chamber 2 and separator 4 connecting pipe, separator 4 discharge pipe. The partial cone chamber 1 is tapered on one side, and the upper part of the other side is cylindrical and the lower part is tapered. The height value is h 1 / h=0.2, there is an opening at the upper and lower ends, the inlet air speed is 10m / s, the outlet air speed is 12m / s, the cross-sectional wind speed is 6m / s; the eccentricity e is e / R 1 = 2, h 1 / h=0.2, h 2 / h=0.6, h / R 1 =4; The spray chamber 2 is a cylindrical hollow structure, the shell is made of steel plate welding, the inlet is frustum-shaped, the outlet is inverted frustum-shaped, the inlet and outlet air speed is 11m / s, the cross-section wind speed is 8m / s, and the height value is h 2 / h=0.6. O 1 It is the center of the welding port of the partial cone cham...

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Abstract

The invention discloses a composite pre-heater, which directly carries out heat exchange and reaction separation between high-temperature gas and low-temperature materials. The composite pre-heater comprises a partial cone chamber (1), a spurting chamber (2) and a separator (4), wherein the lower end of the partial cone chamber (1) is provided with a hot gas inlet, one side of the partial cone chamber (1) is provided with a material spreading valve (6), an opening of the upper end of the partial cone chamber (1) is fixedly connected with an opening of the lower end of the spurting chamber (2), an opening of the upper end of the spurting chamber (2) is fixedly connected with an opening of one side of the separator (4) through a pipeline, a material spreading plate (3) is arranged on the pipeline, the upper part of the material spreading plate (3) is provided with a material inlet, the upper end of the separator (4) is provided with a gas out let, the opening of the lower end of the separator (4) is fixedly connected with the material spreading valve (6) arranged on the partial cone chamber (1) through a pipeline, and a wind locking valve (5) is arranged on the pipeline. Through the partial cone structure, the invention reaches the multidirectional suspension rotation and spurting, and high-temperature materials can not scar and can not be blocked. In the suspension state, the materials have long dwell time through spurting and rotating, and the heat exchange efficiency is high.

Description

Technical field [0001] The invention relates to a gas-solid and liquid-solid heat exchange reaction device, in particular to a composite preheater for direct heat exchange and reaction separation between high temperature gas and low temperature material. Background technique [0002] In cement, chemical and metallurgical production equipment, a device for efficient heat exchange between gas and solid is often required, and equipment with low resistance, no scarring, no clogging, and easy separation of gas and solid, such as a commonly used vertical tube preheater , Cyclone preheater, etc. [0003] Due to its simple structure and low gas ventilation resistance, the vertical tube preheater is suitable for raw materials with high alkali, chlorine and sulfur content. It is not easy to block and does not need bypass; there is no expansion and contraction connection problem, and the amount of air leakage is small; the vertical tube is self-supporting Structure, so the civil construction...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): F27D13/00
Inventor 吕天宝刘飞
Owner 吕天宝
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