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Urea solution hydrolysis reactor

A hydrolysis reactor and solution technology, applied in the field of urea solution hydrolysis reactor, can solve the problems of inability to meet the urea process requirements, high energy consumption, waste of raw materials, etc., and achieve the effects of increased speed, less energy consumption, and less ammonia gas dissolution

Inactive Publication Date: 2015-06-17
XIAN THERMAL POWER RES INST CO LTD +1
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  • Summary
  • Abstract
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  • Claims
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Problems solved by technology

[0004] If urea and water are configured according to the hydrolysis reaction stoichiometric ratio of urea solution, then the mass concentration of urea solution needs to reach 77%, and the urea solution of this concentration must be the supersaturated solution of urea, so the supersaturated solution of urea is used as the hydrolysis reactor Incoming liquid will greatly reduce the content of water vapor at the reactor outlet, but none of the existing reactors can meet the process requirements for accepting urea supersaturated solution, the waste of raw materials is serious, and the energy consumption is relatively large

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  • Urea solution hydrolysis reactor

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Embodiment Construction

[0021] The present invention will be further described in detail below in conjunction with specific embodiments, which are explanations of the present invention rather than limitations.

[0022] Such as figure 1 Shown, a kind of urea solution hydrolysis reactor of the present invention comprises the reactor 1 that urea solution feed inlet 2 and reaction liquid outlet 9 are respectively arranged at the bottom, and the heating device that is arranged in reactor 1 along the urea flow direction successively and Stripping device; the top of the reaction kettle 1 is provided with a reaction gas phase product outlet 5; the stripping device includes a stripping steam inlet 7 connected to the bottom of the reactor 1, and the stripping steam inlet 7 stretches into one end of the reactor 1 Connect stripping steam distributor 11.

[0023] When in use, the urea solution or the supersaturated solution of urea with a mass fraction of 40% to 60% enters the reaction kettle 1 through the urea ...

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Abstract

The invention aims to provide a urea solution hydrolysis reactor which can receive a urea supersaturated solution as an incoming solution to reduce the steam content of an outlet of the reactor, so as to save energy and the consumption of desalted water. The urea solution hydrolysis reactor comprises a reaction kettle of which the bottom part is respectively provided with a urea solution inlet and a reaction liquid outlet, and a heating device and a steam stripping device, wherein the heating device and the steam stripping device are arranged sequentially along the urea flowing direction in the reaction kettle; a reaction gas phase product outlet is formed in the top part of the reaction kettle; the steam stripping device comprises a steam stripping steam inlet communicated to the bottom part of the reaction kettle; one end, extending into the reaction kettle, of the steam stripping steam inlet is connected with a steam stripping steam distributor. By using the steam stripping device, the steam input into the reaction kettle by the steam stripping device is enabled to directly contact the urea solution, in this way, not only is the hydrolysis of the urea solution accelerated, but also the ammonia gas generated in a liquid phase can be accelerated to diffuse continuously into a gas phase and to be output from the reaction gas phase product outlet.

Description

technical field [0001] The invention belongs to the technical field of urea hydrolysis ammonia production equipment in a flue gas denitrification system, and in particular relates to a urea solution hydrolysis reactor. Background technique [0002] Coal combustion in coal-fired power plants is accompanied by large amounts of nitrogen oxides (NO X ) emissions that pollute the atmosphere. Usually, a flue gas denitrification device is installed at the tail of the boiler, and the NO in the flue gas is removed by selective catalytic reduction (SCR). X , converting it into non-toxic and harmless nitrogen (N 2 ) and water (H 2 O), so as to meet the emission requirements. The denitration reducing agent ammonia (NH 3 ) There are usually three supply forms: liquid ammonia, ammonia water and urea. Among them, liquid ammonia and ammonia water are hazardous chemicals. The country has strict laws and regulations concerning the storage, use and transportation of liquid ammonia and a...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C01C1/08
Inventor 徐宏杰林伟杰王月明毕骏白少林牛国平梁法光张波向小凤
Owner XIAN THERMAL POWER RES INST CO LTD
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