Production method of melamine by slow cooling crystallization

A technology of melamine and production methods, applied in the direction of sustainable manufacturing/processing, chemical industry, climate sustainability, etc., can solve the problems of high bituminous coal consumption, large system resistance, large power consumption, etc., and achieve saving power consumption and electricity consumption Effects of reduced coal consumption and reduced system resistance

Inactive Publication Date: 2013-05-15
李鑫
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Problems solved by technology

There are the following problems in production: First, the amount of air-conditioning is generally 4 times the amount of carrier gas, and the preparation of a large amount of air-conditioning requires a lot of power, which seriously affects the power consumption of the product; A large amount of ammonia, carbon dioxide, and a small amount of melamine and urea residues are entrained. The harsh environment can easily cause unstable operation of the fan and frequent shutdowns; third, the cooling and crystallization process of the reaction gas reduces the heat recovery amount and heat recovery grade of the reaction gas. , Improper use of waste heat causes high consumption of bituminous coal; Fourth, the reactor is prone to dead bed, high silica gel breakage rate, uneven bed temperature, and many reaction by-products; Fifth, equipment and pipelines are easy to block, and the oper

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  • Production method of melamine by slow cooling crystallization
  • Production method of melamine by slow cooling crystallization

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Embodiment Construction

[0022] The molten urea is pumped to the urea adding port of the reactor through the urea pump, atomized under the action of the atomizing gas and enters the reactor, under the pressure range from normal pressure to <10MPa and at a high temperature of 390°C, it is reacted and formed by the action of a catalyst Melamine. The heat required for the reaction is provided by the molten salt system. The carrier gas of the fluidized bed comes from the purified and separated reaction tail gas, mainly a mixture of ammonia and carbon dioxide. After the carrier gas compressor is boosted, it is exchanged with the outlet gas of the reactor through a heat exchanger. Heat, and then enter the carrier gas preheater, heated by molten salt to 360-410°C, and then enter the bottom inlet of the reactor.

[0023] The reacted gas enters the heat exchange system to heat the carrier gas at the inlet of the reactor, and its own temperature can be reduced by 310-330°C. The high-boiling point by-products of...

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Abstract

The invention provides a production method of melamine by slow cooling crystallization. The method changes the crystallization process of melamine in a reaction gas and chooses scientific and reasonable multi-functional professional equipment to eliminate a cold air preparation process that has high power consumption and has great influence on production stability. Also, at the same time of reaction gas cooling and melamine crystallization, higher value recovery of reaction gas waste heat is realized, and all production equipment can operate stably for a long period. Thus, the product can have lower power consumption, coal consumption and production cost, and investment in device construction can drop significantly.

Description

technical field [0001] The invention belongs to the technical field of chemical production, in particular to a production method of melamine. Background technique [0002] At present, there are two main dry production processes of melamine: one is the gas phase quenching process; the other is the solid phase quenching crystallization process. [0003] The gas phase quenching process is as follows: the molten urea is pumped to the urea adding port of the reactor through the urine, atomized under the action of the atomizing gas and enters the reactor, and reacts to form melamine under a certain pressure and temperature through the action of a catalyst. . The heat required for the reaction is provided by a molten salt system. The fluidized bed carrier gas entering the reactor comes from ammonia and carbon dioxide mixed gas that is preheated after separation and purification, liquid urine washing and cooling, and compressor boosting. The reacted gas enters the hot gas cooler ...

Claims

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Application Information

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IPC IPC(8): C07D251/60C07D251/62
CPCY02P20/121Y02P20/123Y02P20/124Y02P20/10
Inventor 李鑫
Owner 李鑫
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