A method for recovering and utilizing secondary steam from ammonia distillation
A technology for secondary steam and ammonia distillation, which is applied in the field of recovery and utilization of secondary steam from ammonia distillation, which can solve the problems of resource waste, environmental pollution, and large investment in equipment, and achieve the effects of saving production costs, simple operation, and reducing pollution
- Summary
- Abstract
- Description
- Claims
- Application Information
AI Technical Summary
Problems solved by technology
Method used
Image
Examples
Embodiment 1
[0019] Such as figure 1 As shown, the mother liquor produced in the process of metathesis production of sodium bicarbonate enters the ammonia distillation tower for deammonization treatment. The secondary steam is sent to the condenser for condensation. During the condensation process, the condensation temperature is controlled in the range of 60 to 80 degrees Celsius. The condensate generated in the condenser flows back to the ammonia distillation tower through the return pipe at the bottom of the condenser for deamination again. Treatment, the noncondensable gas containing ammonia and carbon dioxide in the secondary steam of ammonia distillation is drawn out by a vacuum pump and sent to the absorption tower; then, water that can absorb ammonia and carbon dioxide in the noncondensable gas is sent into the absorption tower, and the Ammonia is dissolved in water to obtain ammonia water, which reacts with carbon dioxide to obtain ammonium bicarbonate, so far the absorption liqui...
Embodiment 2
[0023] Such as figure 2 As shown, the difference between this embodiment and Embodiment 1 mainly lies in that a circulation pool is provided, and the water that can absorb ammonia and carbon dioxide in the noncondensable gas is first injected into the circulation pool, and then sent to the absorption tower by the circulation pool, and the water in the absorption tower The discharged absorption liquid also flows into the circulation pool first, and then sent to metathesis production of baking soda by the circulation pool.
[0024] Other process steps of this embodiment are the same as those of Embodiment 1, and will not be repeated here.
Embodiment 3
[0026] Such as image 3 As shown, the difference between this embodiment and embodiment 2 mainly lies in: adding sodium chloride to the water before the water that can absorb ammonia and carbon dioxide in the non-condensable gas is injected into the circulating pool, and the specific way of adding sodium chloride is: set a Dissolving tank, and then put sodium chloride in the dissolving tank, then pour water that can absorb ammonia and carbon dioxide in the non-condensable gas into the dissolving tank and stir, after the sodium chloride in the dissolving tank is dissolved by water, add chlorine The sodium water is injected into the circulation pool, and then the water is sent to the absorption tower from the circulation pool.
[0027] It should be noted that in this embodiment, it is also possible to choose not to add sodium chloride before the water that can absorb ammonia and carbon dioxide in the non-condensable gas is injected into the circulation pool, but after the absorp...
PUM
Login to View More Abstract
Description
Claims
Application Information
Login to View More - R&D
- Intellectual Property
- Life Sciences
- Materials
- Tech Scout
- Unparalleled Data Quality
- Higher Quality Content
- 60% Fewer Hallucinations
Browse by: Latest US Patents, China's latest patents, Technical Efficacy Thesaurus, Application Domain, Technology Topic, Popular Technical Reports.
© 2025 PatSnap. All rights reserved.Legal|Privacy policy|Modern Slavery Act Transparency Statement|Sitemap|About US| Contact US: help@patsnap.com
