Looking for breakthrough ideas for innovation challenges? Try Patsnap Eureka!

Energy-saving ammonia water distillation technology

An ammonia water and steam technology, applied in heating water/sewage treatment, sustainable manufacturing/processing, climate sustainability, etc., can solve the problem of high heat supply, high energy consumption, and water vapor phase transition heat that is not reasonably recycled. and other problems, to achieve the effect of achieving heat balance and reducing the amount of cooling water

Active Publication Date: 2014-03-19
薛斌
View PDF2 Cites 9 Cited by
  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0007] And the place that conventional ammonia water distillation process needs to improve is, the one, need heat source such as a large amount of fresh steams to provide heat for distillation; The 2nd, use a large amount of cooling water to shrink ( Partial condensation cooling, the same below) operation, the phase change heat of water vapor in ammonia vapor has not been properly recovered and utilized, resulting in high external heat supply and high energy consumption required by the process

Method used

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
View more

Image

Smart Image Click on the blue labels to locate them in the text.
Viewing Examples
Smart Image
  • Energy-saving ammonia water distillation technology
  • Energy-saving ammonia water distillation technology
  • Energy-saving ammonia water distillation technology

Examples

Experimental program
Comparison scheme
Effect test

Embodiment approach

[0058] The raw ammonia water at about 75°C after fully standing and filtered by ceramic tubes is heated to about 96°C with the waste water from the bottom of the distillation tower in the ammonia water / waste water heat exchanger, and then enters the upper part of the distillation tower.

[0059] The ammonia vapor (containing hydrogen sulfide, etc.) at about 102°C in the upper part of the distillation tower is condensed and cooled to about 100°C by the circulating waste water in the shrinker, and then sent to the outside of the boundary area for further processing.

[0060] The ammonia distilled waste water at the bottom of the distillation tower at about 105°C is in the ammonia water / waste water heat exchanger, exchanges heat with raw ammonia water and cools down to 86°C, and then enters the evaporator. The 20kPa(a) and 60°C vacuum evaporation steam that escapes from the top of the evaporator enters the MVR steam compressor, and the compressed evaporation steam enters the lower...

Embodiment 1

[0075] The present invention will be further described in detail below in conjunction with the accompanying drawings and embodiments.

[0076] When pressing the ammonia distillation process of accompanying drawing of the present invention, raw material ammonia is earlier exchanged heat with waste water in raw material ammonia water / waste water heat exchanger 6, then in raw material ammonia water / waste water heater 3 and waste water heat exchange or in shrinker 2 After exchanging heat with ammonia vapor, it enters the upper part of distillation tower 1.

[0077] Ammonia vapor (contains H 2 S and HCN and CO 2 and other impurities) escape from the top of the distillation tower, and after being condensed and cooled by circulating waste water or raw ammonia water in the shrinker 2, it is sent to the outside of the boundary area.

[0078]The high-temperature wastewater at the bottom of the distillation tower 1 enters the evaporator 4 for flash evaporation after being cooled by the...

Embodiment 2

[0087] Embodiment 2 (attached figure 2 ):

[0088] The process is similar to Example 1.

[0089] The raw ammonia water from outside the boundary area exchanges heat with the effluent waste water from the evaporator to 70-75°C, and then exchanges heat with the ammonia vapor of the distillation tower in the shrinker to 125-130°C and enters the upper part of the distillation tower. The ammonia vapor at 140°C to 145°C escaping from the top of the distillation tower is condensed and cooled to 90°C to 94°C by the evaporator circulating wastewater and the raw ammonia water in the shrinker, and then the ammonia vapor with a concentration of 13.5% to 14% is sent out of the boundary area. The circulating wastewater from the evaporator is heated by ammonia vapor from 80°C to 85°C to 115°C to 120°C in the shrinker, and then returns to the evaporator to evaporate part of the steam. The wastewater cooled to 88-93°C by raw ammonia water enters the evaporator for flash evaporation. The ev...

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
Login to View More

PUM

No PUM Login to View More

Abstract

The invention provides an energy-saving ammonia water distillation production method which comprises the following steps: (a) providing raw material ammonia water containing NH3 and impurities generated in the production process of chemical enterprises, wherein the impurities comprise H2S, HCN and / or CO2 impurities; (b) performing heat exchange between high-temperature wastewater at the bottom of a distillation tower and the raw material ammonia water and allowing the high-temperature wastewater to enter an evaporator or directly allowing the high-temperature wastewater to enter the evaporator, and performing partial flashing to generate first low-entropy steam, so that the temperature is reduced to be 55-125 DEG C; (c) circulating and feeding the low-temperature wastewater in the evaporator into a dephlegmator, heating the low-temperature wastewater to the temperature of 70-130 DEG C by ammonia steam, returning the wastewater back to the evaporator, and performing partial flashing to generate second low-entropy steam; (d) compressing the obtained first low-entropy steam and second low-entropy steam in the evaporator into saturated high-entropy steam at the temperature of 103-165 DEG C by an MVR (Mechanical Vapor Recompression) compressor, and feeding the saturated high-entropy steam into the distillation tower to serve as a heat supply source for distillation.

Description

technical field [0001] The invention relates to a method for processing raw ammonia water by adopting distillation, evaporation and MVR compression integrated process, especially suitable for the NH-containing NH 3 and H 2 S and HCN, CO 2 Ammonia treatment of raw materials such as impurities. Background technique [0002] According to C (carbon), H (hydrogen), S (sulfur), N (nitrogen), O 2 (Oxygen) and other components are different and the selection of processing technology generates NH in the production process 3 and H 2 S and HCN, CO 2 and other impurities, these impurities are dissolved in water to form raw ammonia water. Although the raw ammonia water itself has little practical value and the cost of treatment is high, the strict requirements of environmental protection do not allow its direct discharge. [0003] In order to solve the outlet of the raw ammonia water, the NH in the raw ammonia water is generally distilled 3 and H 2 S and HCN are separated and re...

Claims

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
Login to View More

Application Information

Patent Timeline
no application Login to View More
IPC IPC(8): C02F1/04
CPCY02P20/10
Inventor 卫宏远
Owner 薛斌
Who we serve
  • R&D Engineer
  • R&D Manager
  • IP Professional
Why Patsnap Eureka
  • Industry Leading Data Capabilities
  • Powerful AI technology
  • Patent DNA Extraction
Social media
Patsnap Eureka Blog
Learn More
PatSnap group products