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Improved production method of ammonia from urea

A technology of urea and urea aqueous solution, which is applied in organic chemical methods, chemical instruments and methods, preparation/separation of ammonia, etc., and can solve problems such as increased energy consumption of reactors

Inactive Publication Date: 2013-04-24
EC&C TECH
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0010] The second issue is the additional heat required to maintain the higher urea concentration in solution
At 40% urea concentration, the heat trace requirement of the urea feed system is reduced but the reactor energy consumption is increased

Method used

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  • Improved production method of ammonia from urea
  • Improved production method of ammonia from urea
  • Improved production method of ammonia from urea

Examples

Experimental program
Comparison scheme
Effect test

example 1

[0085] In Example 1, a 40% feed solution was fed into the reactor or a 40% feed solution was generated in the reactor by feeding urea, concentrated urea and a separate stream of water or steam. (Anhydrous urea is typically granulated and coated with formaldehyde.) A heater is provided to heat the solution in the reactor. Heat input is adjusted to maintain the pressure in the reactor at a set pressure setpoint. Initially, set the pressure set point to start at a value above 30 psia. When heating the reactor to generate 30 psia gas, according to Figure 7 The data shown in set the pressure set point at a pressure corresponding to the reactor temperature. This can be achieved by various methods, such as look-up tables or by fitting Figure 7 Equation calculations for the data in . The desired solubility level, such as 30%, is initially selected for the method. This will provide a large excess of water to the urea and give the solution in the reactor a low salt evolution temp...

example 2

[0092] Example 2 is similar to Example 1 with the exception of figure 1 The temperature demand relationship in and Figure 7 and 8 Find the temperature-pressure relationship for constant water equilibrium in the reactor shown in the ammonia demand-load curve for pressure in this case. Note that using the procedures described in this patent, similar curves and relationships for other feed concentrations can be found or determined by one skilled in the art from the reactor solution concentration at various pressures and temperatures operating at a fixed feed concentration The value determines the relationship used to set the pressure set point as a function of temperature and ammonia production rate. In practice, the operating pressure set point for each fixed load can be manually adjusted and the reactor solution concentration measured. Densitometry can be used to obtain a measure of the concentration of a solution. In this example, the pressure set point is set by substitu...

example 3

[0094] Several users of the current technology use a nominal 70% urea solution obtained prior to granulation or granulation process at the time of urea manufacture. Typically 70% is diluted to 40% to 50% feed concentration. In this Example 3, 70% of the feed was fed to the reactor. Initially the reactor was filled with water such that an initial filling with a 70% solution would result in an initial solution in the reactor showing 40% urea. The product vent gas will be equivalent to a composition of 70% of the feed. In this example the reactor pressure was adjusted such that the water balance in the reactor was maintained at a concentration 40% below the feed concentration. The advantage of this method is that the heat of evaporating water is significantly reduced. In this case, heat consumption was reduced from 4526 Btu / lb ammonia produced to 2193 Btu / lb ammonia. The disadvantage is that with 40% feed solution the 30.5 Compared with the salting-out temperature of 70% fe...

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PUM

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Abstract

A process for generating ammonia from urea, which process comprises: (a) heating an aqueous solution of urea, or a mixture of urea, containing biuret or ammonium carbamate on site, in a hydrolysis reactor such that a gaseous ammonia-containing product is obtained which is essentially free of urea, biuret, or ammonium carbamate, the temperature and pressure being maintained by the input of heat to the reactor; (b) separating the gaseous ammonia-containing product from the liquid phase aqueous reaction media at the operating pressure; (c) retaining the liquid phase reaction medium in the reactor for further conversion to gaseous ammonia and carbon dioxide, and / or recycling at least a portion of the said reaction medium back into the reactor, a urea dissolver, or the feed solution to the reactor for further conversion; and (d) withdrawing the gaseous ammonia and carbon dioxide-containing product separated in step (b) at a controlled rate to meet demand requirements; characterised in that the temperature in the hydrolysis reactor is not controlled but is allowed to vary to match the demand requirement for ammonia and in which the pressure is varied as function of the demand requirement for ammonia or reactor operating temperature. Also claimed is a process for removing nitrogen oxides from a combustion gas stream making use of the ammonia generating process.

Description

technical field [0001] This method requires feeding or generating aqueous urea in a hydrolysis tower (reactor) where it is heated under pressure to produce ammonia, water and carbon dioxide ammonia mixture. In the present invention, it is allowed to vary the reactor operating pressure and temperature to match the ammonia requirement. Reactor pressure is set to vary with ammonia demand or reactor operating temperature. The operating pressure is varied so that during normal operation the concentrations of these gases are in equilibrium with the composition of the solution in the reactor and equal to the conversion products of the feed composition. In a typical process, the feed solution ranges from 40% to 50% by weight urea to water. Background technique [0002] Utilities and A / E companies have shown strong interest in the technology of urea-to-ammonia conversion. Utilities are increasingly adopting urea as the preferred replacement for anhydrous and aqueous ammonia for t...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C01C1/02
CPCY02T10/24F01N2610/02F01N3/208F01N2610/14F01N2900/1814F01N2900/1808F01N2900/1811F01N2240/40C01C1/086F01N2610/10F01N2610/06B01D2251/2062Y02T10/12C01C1/04C07B63/00
Inventor 赫伯特·W·斯潘塞三世H·詹姆斯·彼得斯威廉·G·汉金斯藤田环
Owner EC&C TECH