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

Vapor condensed water recycling process and device for organic amine desulfurization system

A technology of steam condensate and desulfurization system, applied in steam/steam condensers, lighting and heating equipment, etc., can solve the problems of inability to use directly, waste of condensate heat energy and condensate water, and high condensate temperature, so as to achieve reuse , The cost of water production is reduced, and the condensation effect is good.

Inactive Publication Date: 2017-05-31
HUNAN SHUI KOU SHAN NONFERROUS METALS GRP
View PDF6 Cites 0 Cited by
  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0004] The condensed water recovery system in the prior art is to make the condensed water discharged indefinitely from the heating equipment enter the open condensed water tank through the condenser, and finally discharge to nature. It causes waste of heat energy and condensed water, and the temperature of condensed water is high, so it cannot be used directly

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
  • Vapor condensed water recycling process and device for organic amine desulfurization system

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0019] refer to figure 1 : a kind of organic amine desulfurization system of the present embodiment uses steam condensed water recycling process, comprises the following steps:

[0020] After the waste heat steam is utilized by the reboiler of the desulfurization and desorption system, it becomes high-temperature condensed water and enters the steam condensed water tank 1, and then is pumped to the heat exchanger through the condensed water delivery pump 2 to reduce the temperature of the condensed water to 30°C;

[0021] The condensed water passing through the heat exchanger enters the low-temperature condensed water tank 4 for storage, and part of the condensed water in the low-temperature condensed water tank 4 is sent to the ion exchange purification system for use, and the surplus part overflows to the soft water tank and is sent back to the water station for reuse.

[0022] The heat exchange area of ​​the heat exchanger is 10m 2 , the water output of the condensate deli...

Embodiment 2

[0028] The difference with embodiment 1 is:

[0029] The steam generated by the main desulfurization system enters the steam condensed water tank 1, and then is pumped to the heat exchanger through the condensed water delivery pump 2 to reduce the temperature of the condensed water to 30°C;

[0030] The heat exchange area of ​​the heat exchanger is 16m 2 , the output of the condensate delivery pump 2 is 10m 3 / h, the diameter of the refrigerant port is 65mm, and the flow rate is 36 m 3 / h.

[0031] Others are with embodiment 1.

[0032] By adopting the process and device for recycling steam condensed water used in the organic amine desulfurization system of this embodiment, the amount of water produced from desalted water can be reduced by 72,000 tons / year, the cost of water production can be reduced by 835,200 yuan, and the recovery of steam condensed water can reach 72,000 tons / year year.

Embodiment 3

[0034] The difference with embodiment 1 is:

[0035] The steam generated by the main desulfurization system enters the steam condensed water tank 1, and then is pumped to the heat exchanger through the condensed water delivery pump 2 to reduce the temperature of the condensed water to 30°C;

[0036] The heat exchange area of ​​the heat exchanger is 21m 2 , the output of the condensate delivery pump 2 is 15m 3 / h, the diameter of the refrigerant port is 80mm, and the flow rate is 54 m 3 / h.

[0037] Others are with embodiment 1.

[0038] By adopting the process and device for recycling steam condensed water used in the organic amine desulfurization system of this embodiment, the amount of water produced from desalted water can be reduced by 108,000 tons / year, the cost of water production can be reduced by 1,252,800 yuan, and the recovery of steam condensed water can reach 108,000 tons / year year.

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

Disclosed is a vapor condensed water recycling process and device for an organic amine desulfurization system. Vapor is changed into high-temperature condensed water after utilized through a desulfurization and desorption system reboiler to enter a vapor condensed water pot and then is pumped to a heat exchanger. The temperature of the condensed water is decreased to 25-40 DEG C. The condensed water passing through the heat exchanger enters a low-temperature condensed water pot to be stored. Part of the condensed water in the low-temperature condensed water pot is sent to an ion exchanging purifying system to be used. The surplus part of the condensed water overflows to a soft water tank to be sent back into a water production station for recycling. The condensed water is recycled efficiently, the temperature of the condensed water is controlled accurately, the condensation effect is good, the temperature of the condensed water meets the requirement so as to be used directly, and the water production amount and cost are reduced greatly; and demineralized water is replaced with the condensed water, so that the water production amount of the demineralized water can be decreased by 28,800 t / year or above, the water production cost of the demineralized water can be decreased by 334,000 Yuan or above, the vapor condensed water recycling amount reaches up to 28,800 t / year, meanwhile, desulfurization production is not restricted by the demineralized water water-production system, and self-sufficiency is achieved.

Description

technical field [0001] The invention relates to the field of resource recycling, in particular to a process and device for recycling steam condensed water used in an organic amine desulfurization system. Background technique [0002] During the desulfurization process, the absorption and purification system needs desalted water with a conductivity below 5us / cm to remove ions in the water, and the chemical water preparation system often cannot provide desalted water stably. When the water supply is insufficient or the desalinated water preparation system is repaired, it will The soft water preparation system is used as the emergency water source, and the two channels of water use the same pipeline network, which will easily lead to the desulfurization system not being able to continuously start the purification process, and the conductivity of the water must be tested every time the purification is performed, even if this is done, there will still be soft water mixed in the pu...

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): F28B9/08
CPCF28B9/08
Inventor 王辉
Owner HUNAN SHUI KOU SHAN NONFERROUS METALS GRP
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