Urea production process of high-efficiency condensation, low-mounting height CO2 air stripping method and high-voltage lamp type full condensation reactor
A technology of installation height and production process, applied in the field of high-pressure tubular full-condensing reactors, can solve problems such as difficulty in rational utilization, low steam pressure, and short residence time, and achieve the effects of saving investment, convenient operation, and easy maintenance and repair.
Patent Information
- Authority / Receiving Office
- CN · China
- Current Assignee / Owner
- Publication Date
- 2009-07-29
Smart Images
Figure 1 Figure 2 Figure 3
Abstract
Description
technical field
[0001] The invention relates to an industrial urea production process and its special equipment, in particular to a high-efficiency condensation, low installation height CO 2 Gas stripping urea production process and high-pressure tubular full condensation reactor. Background technique
[0002] Industrial urea production is based on CO 2 Gas and liquid ammonia are used as raw materials, which are processed into solid urea products through high-pressure synthesis, medium-pressure or / and low-pressure decomposition and recovery, vacuum concentration, and granulation.
[0003] At present, the production processes of urea plants at home and abroad mainly include the following types: Netherlands Stamicarbon (Stamicarbon) CO 2 Air stripping process, Italian Snamprogetti ammonia stripping process, Japan TEC's ACES21 process, Swiss Casale's high-efficiency synthesis process, aqueous solution full circulation process, etc. Among them, the carbon dioxide stripping pr...
Examples
Embodiment Construction
[0037] Below in conjunction with accompanying drawing, the present invention will be further explained:
[0038] refer to figure 2 , in the high-pressure circle process, will be by CO 2 14.5MPa(A) compressed by the compressor, CO at 120°C 2 Gas, enters high pressure system in two parts, 75-85% CO 2 The gas enters the tube side of the high-pressure stripping tower 3 from the bottom, and the CO of 15-25% 2 The gas enters the urea synthesis tower 2 from the bottom to maintain its thermal balance; the high-pressure stripping tower 3 is a falling film heater, and the shell side is heated with 2.2MPa (A) steam to provide the ammonium carbamate decomposition source from the urea synthesis tower 2. The heat required, the stripping gas generated by the reaction (ie NH 3 and CO 2 Gas) enters the bottom tube side of the high-pressure tubular type total condensation reactor 1 from the top outlet of the high-pressure stripping tower 3 tube sides; NH in synthesis tower 2 3 and CO 2...