Method for orderly rectifying and separating nitromethane-nitroethane-nitropropane by continuous three towers

A technology of nitropropane and nitromethane, which is applied in the field of continuous three-tower sequential distillation and separation of nitromethane-nitroethane-nitropropane, which can solve the problem of low market demand, no large-scale production, and complicated operation process And other issues

Inactive Publication Date: 2011-11-02
NANJING NORMAL UNIVERSITY
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Problems solved by technology

Nitromethane has only semi-industrial scale production facilities in China. The production method is mainly nitrite replacement method. The product price varies with the quality, and most of them are exported; It is widely used in the synthesis of pesticides. At present, there is only small-scale production in China, and the content of the product is as high as 99%. Due to the difficulty in production and high risk, some manufacturers have stopped production one after another. There is no large-scale production in China, and they basically rely on imports; Similar to nitroethane, nitropropane has not yet formed a large-scale production in China due to its complicated process and low market demand.
[0004] At present, the separation of nitroalkane mixtures generally adopts multiple distillations to obtain a single fraction. Due to the small difference in boiling point between the low-carbon nitroalkane components, the properties of the components are shown in Table 1, and the distillation method is used for separation. Not only is the operation process complicated , Difficult to control, low product purity, and too many middle distillates at the same time, the yield can only reach 53%

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  • Method for orderly rectifying and separating nitromethane-nitroethane-nitropropane by continuous three towers
  • Method for orderly rectifying and separating nitromethane-nitroethane-nitropropane by continuous three towers
  • Method for orderly rectifying and separating nitromethane-nitroethane-nitropropane by continuous three towers

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Embodiment Construction

[0019] The present invention is described in detail below in conjunction with specific embodiment, described embodiment helps to the understanding and implementation of the present invention, does not constitute limitation of the present invention, implements the present invention, except the material involved in the specific embodiment and rectifying operation In addition to conditions, those skilled in the art can also perform equivalent or equivalent transformations according to different separation purposes. The protection scope of the present invention is not limited by the specific embodiments, but by the claims. Unless otherwise specified, the percentages in the present invention are all mass percentages.

[0020] A method for the sequential rectification of three consecutive towers to separate nitromethane-nitroethane-nitropropane, refer to figure 1 Shown technology and parameter shown in table 2, raw material (1) is the mixed liquor of nitromethane, nitroethane, 2...

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Abstract

The invention relates to a method for orderly rectifying and separating nitromethane-nitroethane-nitropropane by continuous three towers, the raw material (an mixed solution of nitromethane, nitroethane,2-nitropropane and 1-nitropropane) is separated through a first continuous rectifying tower at first(B1), the content of the separated nitromethane on the top of the tower can reach over 99.5%, a distillate from the bottom is separated through the second continuous rectifying tower (B2), the content of the separated 1-nitropropane at the bottom of the tower can reach over 99.5%, the once through yields are respectively reach to 89.7% and 91.2%; a distillate from top of a second continuous rectifying tower (B2) is entered into a third continuous rectifying tower (B3) for separating nitroethane and 2-nitropropane, the content of nitroethane can reach above 82.0%, the content of 2-nitropropane can reach above 87.0%. Compared with the multi-times distillation method in the prior art, the separated product content and yield rate of the method provided in the invention are higher than that of the multi-times distillation method.

Description

technical field [0001] The invention relates to a chemical separation process, in particular to a method for sequential rectification and separation of nitromethane-nitroethane-nitropropane in three consecutive towers. Background technique [0002] Low-carbon nitroalkanes are important solvents and intermediates. Nitromethane is mainly used as a solvent and gasoline additive; nitroethane is used in organic synthesis, as a solvent for nitrocellulose and other resins, waxes, fats, dyes, etc. ; Nitropropane includes 1-nitropropane and 2-nitropropane, 2-nitropropane is used as a special solvent for ethylene and epoxy resin coatings, rocket fuel, gasoline additives, etc., and is also used in organic synthesis; 1- Nitropropane is mainly used as solvents and intermediates, jet engine fuels, sprays, etc. (1) As a solvent, it has strong resistance to alcohols, ketones, ethers, esters, dyes, greases, waxes, resins, and synthetic rubbers. Solubility, used together with alcohol is a st...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C07C205/02C07C201/16
Inventor 顾正桂
Owner NANJING NORMAL UNIVERSITY
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