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Freon treated by premixed combustion and method for producing said resource

A pre-mixed combustion and freon technology, applied in the direction of combustion method, combustion type, incinerator, etc., can solve the problems of unstable freon decomposition rate, low carbon dioxide selectivity, incomplete freon decomposition, etc., to improve flame propagation speed and combustion Effects of increasing temperature and decomposition rate and reducing fuel consumption

Inactive Publication Date: 2008-09-03
KUNMING UNIV OF SCI & TECH
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

On the one hand, the mixing of the reactant and the combustion flame is greatly affected under this condition, and the direct injection of cold to-be-processed material makes the flame stability worse, and these factors will directly lead to the instability of the decomposition rate of Freon; on the other hand On the one hand, although the idea of ​​spraying the reactants to the burning flame is simpler, the reactants do not participate in the process of fuel heating to combustion, and the time of the reactants in the high temperature zone is greatly shortened, which is beneficial for the reactant molecules to obtain energy. The activation process is extremely unfavorable. In order to achieve a higher decomposition rate, more fuel must be supplied, which wastes precious energy.
[0003] In addition, the patent document CN1049295A discloses a catalytic decomposition method of chlorofluoroalkanes, which uses a catalyst containing alumina or alumina-silicon dioxide, which can decompose Freon at a relatively low temperature and in the presence of water vapor, but The serious problem of this method is that the life of the catalyst is very short, and the hydrogen fluoride produced by the decomposition of freon has a strong fluorination effect on the aluminum oxide, causing the catalyst to be obviously deactivated within a few hours; and when the treatment content is higher than 5% When freon gas is used, the selectivity of the reaction to generate carbon dioxide is greatly reduced, and the decomposition of freon is not complete, which is also a common problem in the current catalytic decomposition of freon

Method used

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  • Freon treated by premixed combustion and method for producing said resource
  • Freon treated by premixed combustion and method for producing said resource
  • Freon treated by premixed combustion and method for producing said resource

Examples

Experimental program
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Effect test

Embodiment 1

[0040] Commercially available Freon-12 (F-12, namely difluorodichloromethane CCl 2 f 2 ). For Freon-12, m, n, and p in formula (a) are 1, 0, and 4 respectively, then formula (a) becomes:

[0041] CCl 2 f2 +2H 2 O→CO 2 +2HF+2HCl (c)

[0042] Use civil liquefied petroleum gas as fuel.

[0043] The incinerator cavity is a cylindrical cavity with a diameter of 120mm and a length of 1000mm.

[0044] The flow velocity of the premixed gas in the heat exchange tube is 5.6M / s, and the flow velocity of the combustion exhaust gas in the premixer is 1.5M / s.

[0045] First of all, according to the design processing capacity range of the incinerator, the processing capacity of Freon is determined to be 0.01M 3 / min; According to formula (1), it is determined that Freon: the molar ratio of fuel = 1: 1, that is, the liquefied petroleum gas flow rate is 0.01M 3 / min; determined according to formula (2) That is, the water vapor flow rate is 0.005M 3 / min; 1M 3 The theoretical air v...

Embodiment 2

[0051] Commercially available Freon-13 (F-13, that is, trifluorochloromethane CClF 3 ). For Freon-13, m, n, and p in formula (a) are 1, 0, and 4 respectively, and formula (a) is:

[0052] CCIF 3 +2H 2 O→CO 2 +3HF+HCl (d)

[0053] Use artificial gas (the main component is carbon monoxide) as fuel.

[0054] Incinerator is the same as embodiment 1.

[0055] First of all, according to the design processing capacity range of the incinerator, the processing capacity of Freon is determined to be 0.012M 3 / min, according to formula (1) to determine Freon: fuel molar ratio = 1: 7.5, that is, the artificial gas flow rate is 0.09M 3 / min, determined according to formula (2) That is, the water vapor flow rate is 0.036M 3 / min, 1M 3 The theoretical air volume required for artificial gas combustion is 18.51M 3 , taking the excess air coefficient of liquefied petroleum gas combustion as 1.1, and the primary air volume accounts for 70% of the total air volume, the total air volume...

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Abstract

This invention relates to one method to pre-mix fuel for chlorofluoromethane and its materials, which comprises the following steps: mixing the reactor chlorofluoromethane, water, fuel and air for heating up to improve reaction molecule energy and to improve fuel heating speed; mixture gas pre-heating makes burst furnace temperature lift helpful for back reactions; using fuel tail fuel gas and air to improve flare transmission speed and temperature to add burst intensity and to improve device heat efficiency.

Description

1. Technical field [0001] The invention relates to a method for premixed combustion treatment of freon and its resource recovery, which belongs to the technical field of metallurgy and chemical industry. 2. Background technology [0002] Freon (CFCs) is a large-scale industrial production of compounds containing four elements of fluorine, chlorine, carbon, and hydrogen or only three elements of fluorine, chlorine, and carbon. Its chemical properties are very stable, non-toxic or low-toxic, and non-corrosive Non-combustible, mostly non-flammable, widely used in refrigerants, foaming agents, sprays, cleaning agents and other fields. However, it is precisely because of their excellent stability that they are difficult to degrade after being discharged into the atmosphere. When they rise to the stratosphere, under the action of ultraviolet rays, they will produce catalytic species that can decompose ozone molecules, thereby destroying the ozone layer. They not only destroy the ...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): F23G7/06F23J15/02
Inventor 宁平高红刘天成张永马林转邹金宝
Owner KUNMING UNIV OF SCI & TECH
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