CN205867621U - Decompression multiple -effect glass evaporimeter system - Google Patents
Decompression multiple -effect glass evaporimeter system Download PDFInfo
- Publication number
- CN205867621U CN205867621U CN201620183138.4U CN201620183138U CN205867621U CN 205867621 U CN205867621 U CN 205867621U CN 201620183138 U CN201620183138 U CN 201620183138U CN 205867621 U CN205867621 U CN 205867621U
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- China
- Prior art keywords
- condenser
- evaporimeter
- column tube
- inlet pipe
- pipe
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- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
Abstract
The utility model discloses a decompression multiple -effect glass evaporimeter system, including evaporator unit and cooling device, evaporator unit includes condenser and a plurality of groups tubulation evaporimeter, the tubulation evaporimeter sets up in condenser one side, cooling device passes through cyclone and links to each other with condenser and tubulation evaporimeter. The utility model has the advantages that: equipment adopts the decompression evaporation, forms certain vacuum state in the evaporating pipe, and the temperature of effectual reduction feed liquid boiling point has reduced the energy consumption of equipment operation, utilize flash steam effectively to preheat and reuse simultaneously, reduce and give birth to the steam quantity, reduce the energy consumption. The utility model discloses a reduce the emission of waste water to the evaporative concentration of waste water, realize resource recycling.
Description
Technical field
This utility model relates to evaporation equipment, is specifically related to a kind of decompression multiple-effect glass evaporators system.
Background technology
Along with the fast development of the industries such as plating, chemical industry, pharmacy, smelting, papermaking, the industrial wastewater of generation is the most increasingly
Many, in waste water, harmful substance contents is high, complicated component, thus results in treatment technology difficulty relatively big, and causes surrounding sternly
The threat of weight.Along with the raising day by day of mankind's environmental consciousness, waste water is innoxious and recycling treatment is increasingly closed by people
Note and attention.It is to process one of effective method of waste water that industrial wastewater is evaporated concentrating and separating, permissible by evaporation and concentration
Reclaim useful resource, greatly reduce the pollution to environment.
Utility model content
This utility model is for the problems referred to above, it is provided that a kind of thickening efficiency is high, volume is little, the decompression multiple-effect that can reuse
Glass evaporators system.
The technical scheme in the invention for solving the above technical problem is:
A kind of decompression multiple-effect glass evaporators system, including evaporator and chiller, described evaporator bag
Including condenser and some groups of column tube evaporimeters, described column tube evaporimeter is arranged on condenser side, and described chiller is by rotation
Wind separator is connected with condenser and column tube evaporimeter.
Further, described condenser includes condenser body, described condenser this most internal be provided with the first condenser and the
Two condensers, described condenser body side is provided with feed pipe, discharge nozzle, cooling water inlet pipe and cooling water outlet tube, described charging
Pipe is connected with discharge nozzle and the first condenser, and described cooling water inlet pipe is connected with cooling water outlet tube and the second condenser, described cold
The top of condenser body is provided with air inlet pipe, and the bottom of described condenser body is provided with condensed water and goes out pipe.
Further, described column tube evaporimeter sidepiece is provided with steam inlet tube and condensation-water drain, described column tube evaporimeter
Top is provided with concentrated solution outlet, and the bottom of described column tube evaporimeter is provided with fluid-tight device.
Further, described some groups of column tube evaporimeters pass sequentially through cyclone separator and connect, and described discharge nozzle passes through
The fluid-tight device of pipeline and first group of column tube evaporimeter connects, and described concentrated solution outlet is steamed with next group tubulation by cyclone separator
The steam inlet tube sending out device is sequentially connected with fluid-tight device.
Further, described chiller includes cooling cylinder, is provided with coolant inlet pipe and coolant outside described cooling cylinder
Going out pipe, described cooling cylinder upper end is provided with concentrated solution inlet pipe, and described cooling cylinder lower end is provided with concentrated solution and goes out pipe.
Further, the concentrated solution inlet pipe of described cooling cylinder by the air inlet pipe of cyclone separator and condenser body with
And the concentrated solution outlet of column tube evaporimeter is connected.
The utility model has the advantages that: equipment uses and is evaporated under reduced pressure, and forms certain vacuum state, effectively in evaporation tube
The temperature of reduction feed liquid boiling point, reduce the energy consumption that equipment runs；Utilize indirect steam effectively to preheat and again simultaneously
Utilize, reduce raw steam consumption, reduce energy consumption.This utility model by reducing the discharge of waste water to the evaporation and concentration of waste water, real
Existing resource recycling.
Accompanying drawing explanation
Constitute the part of this specification, be used for being further appreciated by accompanying drawing of the present utility model and show of the present utility model
Preferred embodiment, and be used for principle of the present utility model is described together with description.
Fig. 1 is the structural representation of this utility model embodiment 1；
Fig. 2 is the structural representation of this utility model embodiment 2.
Wherein, reference:
100 it is evaporator, 110 is condenser, 111 is condenser body, 112 is the second condenser, 113 is second
Condenser, 114 be feed pipe, 115 for discharge nozzle, 116 for cooling water inlet pipe, 117 for cooling water outlet tube, 118 for air inlet pipe,
119 for condensed water go out pipe, 120 be column tube evaporimeter, 121 be steam inlet tube, 122 be condensation-water drain, 123 go out for concentrated solution
Mouthful, 124 for fluid-tight device, 200 for chiller, 210 for cooling cylinder, 211 for coolant inlet pipe, 212 for coolant go out manage, 213
For concentrated solution inlet pipe, 214 for concentrated solution go out pipe.
Detailed description of the invention
Below in conjunction with accompanying drawing, embodiment of the present utility model is described in detail, but this utility model can be by right
Require that the multitude of different ways limiting and covering is implemented.
Embodiment 1
With reference to Fig. 1, a kind of decompression multiple-effect glass evaporators system as shown in Figure 1, including evaporator 100 and cooling
Device 200, described evaporator 100 includes condenser body 110 and 2 groups of column tube evaporimeters 120, described column tube evaporimeter
120 are arranged on condenser body 110 side, described chiller 200 by cyclone separator 300 and condenser body 110 and
Column tube evaporimeter 120 is connected.
Described condenser 110 includes condenser body 111, be provided with in described condenser body 111 first condenser 112 with
Second condenser 113, described condenser body 111 sidepiece is provided with feed pipe 114, discharge nozzle 115, cooling water inlet pipe 116 and cold
But water goes out pipe 117, described feed pipe 114 and discharge nozzle 115 and is connected 112 with the first condenser, described cooling water inlet pipe 116 and cold
But water goes out pipe 117 and is connected with the second condenser 113, and the top of described condenser body 111 is provided with air inlet pipe 118, described condensation
The bottom of device body 111 is provided with condensed water and goes out pipe 119.
Described column tube evaporimeter 120 sidepiece is provided with steam inlet tube 121 and condensation-water drain 122, described column tube evaporimeter 120
Top be provided with concentrated solution outlet 123, the bottom of described column tube evaporimeter 120 is provided with fluid-tight device 124.
Described 2 groups of column tube evaporimeters 120 pass sequentially through cyclone separator 300 and connect, described discharge nozzle 115 by pipeline with
The fluid-tight device 124 of the column tube evaporimeter 120 of first group connects, described concentrated solution outlet 123 by cyclone separator 300 and next
The steam inlet tube 121 of group column tube evaporimeter 120 is sequentially connected with fluid-tight device 124.
Described chiller 200 includes cooling cylinder 210, is provided with coolant inlet pipe 211 and cooling outside described cooling cylinder 210
Liquid goes out pipe 212, and described cooling cylinder 210 upper end is provided with concentrated solution inlet pipe 213, and described cooling cylinder 210 lower end is provided with concentrated solution and goes out pipe
214。
The concentrated solution inlet pipe 213 of described cooling cylinder 210 air inlet pipe by cyclone separator 300 with condenser body 111
118 and the concentrated solution outlet 123 of column tube evaporimeter 120 of end be connected.
Embodiment 2
As in figure 2 it is shown, a kind of decompression multiple-effect glass evaporators system, including evaporator 100 and chiller 200,
Described evaporator 100 includes condenser 110 and 3 groups of column tube evaporimeters 120, and described column tube evaporimeter 120 is arranged on condensation
Device 110 side, described chiller 200 is connected with condenser 110 and column tube evaporimeter 120 by cyclone separator 300.
Described condenser 110 includes condenser body 111, be provided with in described condenser body 111 first condenser 112 with
Second condenser 113, described condenser body 111 sidepiece is provided with feed pipe 114, discharge nozzle 115, cooling water inlet pipe 116 and cold
But water goes out pipe 117, described feed pipe 114 and discharge nozzle 115 and is connected 112 with the first condenser, described cooling water inlet pipe 116 and cold
But water goes out pipe 117 and is connected with the second condenser 113, and the top of described condenser body 111 is provided with air inlet pipe 118, described condensation
The bottom of device body 111 is provided with condensed water and goes out pipe 119.
Described column tube evaporimeter 120 sidepiece is provided with steam inlet tube 121 and condensation-water drain 122, described column tube evaporimeter 120
Top be provided with concentrated solution outlet 123, the bottom of described column tube evaporimeter 120 is provided with fluid-tight device 124.
Described 3 groups of column tube evaporimeters 120 pass sequentially through cyclone separator 300 and connect, described discharge nozzle 115 by pipeline with
The fluid-tight device 124 of first group of column tube evaporimeter 120 connects, and described concentrated solution outlet 123 is by cyclone separator 300 and next group
The steam inlet tube 121 of column tube evaporimeter 120 is sequentially connected with fluid-tight device 124.
Described chiller 200 includes cooling cylinder 210, is provided with coolant inlet pipe 211 and cooling outside described cooling cylinder 210
Liquid goes out pipe 212, and described cooling cylinder 210 upper end is provided with concentrated solution inlet pipe 213, and described cooling cylinder 210 lower end is provided with concentrated solution and goes out pipe
214。
The concentrated solution inlet pipe 213 of described cooling cylinder 210 air inlet pipe by cyclone separator 300 with condenser body 111
118 and the concentrated solution outlet 123 of column tube evaporimeter 120 be connected.
Specific works mode:
By outside pumped vacuum systems, condenser body being carried out evacuation and form negative pressure, waste water enters from feed pipe,
Preheat through the first condenser, then flow into fluid-tight device by pipeline, then carry out heating evaporation by column tube evaporimeter, then
Carrying out vapor-liquid separation through cyclone separator, gas is up as the heating steam of next group column tube evaporimeter, and solution is toward dirty
Enter fluid-tight device, then in next column tube evaporimeter, carry out heating evaporation, such multistage cascade evaporation, evaporate to final evaporator
Being concentrated into desired concn, be then passed through cyclone separator and separate, concentrated solution flows downstream into chiller and flows out, through supercooling
After concentrated solution and condensed water collect respectively.
These are only preferred embodiment of the present utility model, be not limited to this utility model, for this area
Technical staff for, this utility model can have various modifications and variations.It is all within spirit of the present utility model and principle,
Any modification, equivalent substitution and improvement etc. made, within should be included in protection domain of the present utility model.
Claims (6)
1. a decompression multiple-effect glass evaporators system, including evaporator (100) and chiller (200), its feature exists
In, described evaporator (100) includes condenser (110) and some groups of column tube evaporimeters (120), described column tube evaporimeter
(120) being arranged on condenser (110) side, described chiller (200) is by cyclone separator (300) and condenser (110)
It is connected with column tube evaporimeter (120).
Decompression multiple-effect glass evaporators system the most according to claim 1, it is characterised in that described condenser (110) wraps
Include condenser body (111), in described condenser body (111), be provided with the first condenser (112) and the second condenser (113),
Described condenser body (111) sidepiece is provided with feed pipe (114), discharge nozzle (115), cooling water inlet pipe (116) and cooling water and goes out
Pipe (117), described feed pipe (114) is connected (112) with the first condenser with discharge nozzle (115), described cooling water inlet pipe (116)
Being connected with the second condenser (113) with cooling water outlet tube (117), the top of described condenser body (111) is provided with air inlet pipe
(118), the bottom of described condenser body (111) be provided with condensed water go out pipe (119).
Decompression multiple-effect glass evaporators system the most according to claim 2, it is characterised in that described column tube evaporimeter
(120) sidepiece is provided with steam inlet tube (121) and condensation-water drain (122), and the top of described column tube evaporimeter (120) is provided with concentration
Liquid outlet (123), the bottom of described column tube evaporimeter (120) is provided with fluid-tight device (124).
Decompression multiple-effect glass evaporators system the most according to claim 3, it is characterised in that described some groups of tubulations evaporation
Device (120) passes sequentially through cyclone separator (300) and connects, and described discharge nozzle (115) passes through pipeline and first group of column tube evaporimeter
(120) fluid-tight device (124) connects, and described concentrated solution outlet (123) is evaporated with next group tubulation by cyclone separator (300)
The steam inlet tube (121) of device (120) is sequentially connected with fluid-tight device (124).
Decompression multiple-effect glass evaporators system the most according to claim 4, it is characterised in that described chiller (200)
Including cooling cylinder (210), described cooling cylinder (210) outside is provided with coolant inlet pipe (211) and coolant goes out pipe (212), described
Cooling cylinder (210) upper end is provided with concentrated solution inlet pipe (213), and described cooling cylinder (210) lower end is provided with concentrated solution and goes out pipe (214).
Decompression multiple-effect glass evaporators system the most according to claim 5, it is characterised in that described cooling cylinder (210)
Concentrated solution inlet pipe (213) is by cyclone separator (300) and the air inlet pipe (118) of condenser body (111) and the row of end
The concentrated solution outlet (123) of pipe evaporator (120) is connected.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620183138.4U CN205867621U (en) | 2016-03-10 | 2016-03-10 | Decompression multiple -effect glass evaporimeter system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620183138.4U CN205867621U (en) | 2016-03-10 | 2016-03-10 | Decompression multiple -effect glass evaporimeter system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205867621U true CN205867621U (en) | 2017-01-11 |
Family
ID=57687872
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201620183138.4U Expired - Fee Related CN205867621U (en) | 2016-03-10 | 2016-03-10 | Decompression multiple -effect glass evaporimeter system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205867621U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105817046A (en) * | 2016-03-10 | 2016-08-03 | 浙江重氏环境资源有限公司 | Reduced pressure multi-effect glass evaporator system |
-
2016
- 2016-03-10 CN CN201620183138.4U patent/CN205867621U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105817046A (en) * | 2016-03-10 | 2016-08-03 | 浙江重氏环境资源有限公司 | Reduced pressure multi-effect glass evaporator system |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20170111 |