CN209325761U - Feed Manufacturing steam condensate recovery system - Google Patents
Feed Manufacturing steam condensate recovery system Download PDFInfo
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- CN209325761U CN209325761U CN201821653057.1U CN201821653057U CN209325761U CN 209325761 U CN209325761 U CN 209325761U CN 201821653057 U CN201821653057 U CN 201821653057U CN 209325761 U CN209325761 U CN 209325761U
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- granulator
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Abstract
The utility model discloses Feed Manufacturing steam condensate recovery systems; gas-distributing cylinder is connected to by steam pipe a with granulator; steam-water separator a is provided on steam pipe a; gas-distributing cylinder is connected to by condensate pipe a with water tank; steam-water separator b is provided on condensate pipe a; water tank is connected by pipeline with boiler, and boiler is connected by steam pipe b with gas-distributing cylinder, and the steam-water separator a is connected to by condensate pipe b with condensate pipe a.The system can realize the effect of automatic recycling condensed water, reduce the waste of condensed water, play preferable energy conservation, water-saving effect；It ensure that be uniformly dispersed degree of the air-flow in granulator, so that moist material will not influence granulate quality and granulation efficiency due to being adhered in granulator inner wall in granulator, while also ensuring the uniformity of granulation.
Description
Technical field
The utility model belongs to feed production technology field, and in particular to Feed Manufacturing steam condensate recovery system.
Background technique
In the production process of feed, many processes need the steam generated with boiler to be produced, then cooling
A large amount of condensed water can be generated in the process, how water process is condensed to these, traditional method is complicated simply by direct emission
Any needs the reuse again after natural cooling or pressure are cooling again, these treating methods all can waste of energy.In addition, due to producing
The pressure of raw high-temperature steam, condensed water is different, if with normal use without pressure water by same pipeline, it may
It will cause pipeline to burst apart or other perils；However, if by extra water and extra steam direct emission, due to equipment
The steam or coolant-temperature gage of generation are higher, are likely to result in underground piping damage or cause thermal pollution to environment.Therefore, how to research and develop
A kind of Feed Manufacturing steam condensate recovery system, has important practical significance.
Utility model content
Lead to waste of energy for the direct outlet of condensed water generated in feed preparation existing in the prior art
Technical problem, the purpose of this utility model is to provide Feed Manufacturing steam condensate recovery systems.
The technical solution that the utility model is taken are as follows:
Feed Manufacturing steam condensate recovery system, including granulator, gas-distributing cylinder, water tank and boiler, gas-distributing cylinder pass through
Steam pipe a is connected to granulator, and steam-water separator a is provided on steam pipe a, and gas-distributing cylinder is connected to by condensate pipe a with water tank,
Steam-water separator b is provided on condensate pipe a, water tank is connected by pipeline with boiler, and boiler is connected by steam pipe b and gas-distributing cylinder
It connects, the steam-water separator a is connected to by condensate pipe b with condensate pipe a.
Further, it is provided with air blower on the outside of the granulator, air blower is connected with jet-stream wind pipe, jet-stream wind
The arrival end of pipe extends to the bottom of granulator.
Further, the arrival end of the jet-stream wind pipe is provided with jet-stream wind guide plate, jet-stream wind guide plate
It is set as the guide plate a and guide plate b of two panels tile, the curved wall of guide plate a and guide plate b is opposite and the certain water conservancy diversion gap row in interval
Cloth forms.
Further, the upper end of the jet-stream wind guide plate is provided with gas distributor, and gas distributor includes water
Horizontal disk is put down, disk surrounding is connected with the inner wall of air blower, and disc surfaces are uniformly provided with gas port.
Further, the corresponding position of each gas port on the disk is provided with water conservancy diversion paddle, the setting of water conservancy diversion paddle
For arc paddle blade structure, the free end of water conservancy diversion paddle is to helically arc-shaped bend extends at disc centre.
Further, the water tank is internally provided with floating-ball level switch.
The utility model has the following beneficial effects:
Steam in boiler is applied in granulator granulation by the utility model, simultaneously by adding steam-water separator
Condensed water is recycled by condensing water conduit with gas-distributing cylinder, storage is again in water tank, and condensate temperature is higher, after being sent to boiler
The energy required when heating will be reduced, the waste of water is reduced, plays preferable energy conservation, water-saving effect；System design is reasonable,
It can ensure that water tank can collect the condensed water that condensate pipe is sent at any time, realize the effect of automatic recycling condensed water；In granulator
Jet-stream wind pipe and gas distributor, the air-flow of air blower is uniformly distributed, ensure that air-flow in granulator point
Uniformity coefficient is dissipated, so that moist material will not influence granulate quality and granulation due to being adhered in granulator inner wall in granulator
Efficiency, while also ensuring the uniformity of granulation.
Detailed description of the invention
Fig. 1 is the overall structure diagram of the utility model.
Fig. 2 is the schematic diagram of internal structure of granulator in the utility model.
Wherein, 1, granulator；2, steam-water separator a；3, gas-distributing cylinder；4, steam-water separator b；5, water tank；6, boiler；7, into
Expects pipe；8, gas distributor；9, jet-stream wind guide plate；10, jet-stream wind pipe；11, air blower.
Specific embodiment
The utility model is further illustrated with reference to the accompanying drawing.
Embodiment 1
As shown in Figure 1, Feed Manufacturing steam condensate recovery system, including granulator 1, gas-distributing cylinder 3, water tank 5 and pot
Furnace 6, gas-distributing cylinder 3 are connected to by steam pipe a with granulator 1, and steam-water separator a2 is provided on steam pipe a, and gas-distributing cylinder 3 passes through cold
Condensate pipe a is connected to water tank 5, and steam-water separator b4 is provided on condensate pipe a, and water tank 5 is connected by pipeline and boiler 6, pot
Furnace 6 is connected by steam pipe b and gas-distributing cylinder 3, and the steam-water separator a2 is connected to by condensate pipe b with condensate pipe a.
Carrying out practically process are as follows: the high steam that reaction generates in boiler 6 is exported along steam pipe b to 3 (carbonated drink of gas-distributing cylinder
Separator) at, density contrast of the gas-distributing cylinder 3 using vapour and water, Lai Shixian steam-water separation；By the isolated vapour of gas-distributing cylinder 3
Body enters in steam-water separator a2 along steam pipe a further to be separated, steam-water separator a2 steam is further separated formed it is cold
Condensate and steam, steam, which continues on steam pipe a and is passed directly into granulator 1, pelletizes；It is separated by steam-water separator a2
Obtained condensed water is directly entered in water tank 5 along condensate pipe b circulation and stores；Condensed water after the separation of gas-distributing cylinder 3 is along cold
Condensate pipe a enters steam-water separator b4, and steam-water separator b4 separates condensed water further progress, and steam-water separator b4 is separated
To condensed water flow into water tank 5 and stored along condensate pipe a；Steam-water separator b4 isolated steam is passed into
In steam pipe b, and then it is delivered in gas-distributing cylinder 3.
It realizes and recycles by the condensed water that above system is stored in water tank 5, avoid causing due to pressure difference
Pipeline breaking or steam leakage, to effectively improve the rate of recovery of condensed water；And it avoids the condensed water or steam of higher temperature
Phenomena such as direct emission causes underground piping to damage or cause thermal pollution to environment.
Embodiment 2
On the basis of embodiment 1, it is different from embodiment 1, as shown in Fig. 2, the outside of granulator 1 is provided with air blower
11, air blower 11 and jet-stream wind pipe 10 connect, and the arrival end of jet-stream wind pipe 10 extends to the bottom of granulator 1, granulator 1
Top be provided with feed pipe 7, the lower section of feed pipe 7 is arranged in jet-stream wind pipe 10.
The arrival end of jet-stream wind pipe 10 is provided with jet-stream wind guide plate 9, and jet-stream wind guide plate 9 is set as two panels watt
The curved wall of the guide plate a and guide plate b of sheet, guide plate a and guide plate b are opposite and the certain water conservancy diversion void arrangement in interval forms.Tile
9 structure novel of jet-stream wind guide plate of shape, and play the role of convergence guiding to the air-flow flowed through, it ensure that air-flow to upload
The stability led.
The upper end of jet-stream wind guide plate 9 is provided with gas distributor 8, and gas distributor 8 includes horizontal horizontal disk,
Disk surrounding is connected with the inner wall of air blower 11, and disc surfaces are uniformly provided with gas port.The disk for opening up gas port is convenient for
The effect for being uniformly distributed and being oriented to air-flow ensure that air-flow in the evenly dispersed cavity to granulator 1, ensure that system
The uniformity of grain.
The corresponding position of each gas port on disk is provided with water conservancy diversion paddle, and water conservancy diversion paddle is set as arc paddle blade structure,
The free end of water conservancy diversion paddle is to helically arc-shaped bend extends at disc centre.The arcuate guide of water conservancy diversion paddle acts on, can be to air-flow
Play the role of arcuate guide, is quickly transferred to air-flow in gas port and is dispersed, avoid blocking phenomenon.
Water tank 5 is internally provided with floating-ball level switch, and floating-ball level switch and alarm are connected with each other, and passes through Floating Ball Liquid Level
Switch real-time detection water tank 5 inside level condition, when the liquid level inside water tank 5 reaches highest liquid level, by alarm into
Row alarm can carry out water conservancy diversion outlet by other pipelines to the condensed water inside water tank 5, ensure that the operation stability of system.
Carrying out practically process are as follows:
Starting air blower 11, air blower 11 carries out air blast to granulator 1, and gas enters granulator 1 from jet-stream wind pipe 10,
The jet-stream wind guide plate 9 of 10 arrival end of jet-stream wind pipe forms the effect of certain convergence water conservancy diversion to air-flow, ensure that injection
Air-flow transmits upwards along the water conservancy diversion gap of jet-stream wind guide plate 9, and is redistributed via gas distributor 8, gas point
Water conservancy diversion paddle on cloth device 8 forms stable guide functions to air-flow, it is ensured that air-flow disperses upwards along the stomata on disk, protects
The degree that is uniformly dispersed of air-flow is demonstrate,proved, so that moist material will not be influenced due to being adhered in 1 inner wall of granulator in granulator 1
Granulate quality and granulation efficiency, while also ensuring the uniformity of granulation.
The above is not limitations of the present invention, it should be pointed out that: for the ordinary skill people of the art
For member, under the premise of not departing from the utility model in essence range, several variations, modifications, additions or substitutions can also be made,
These improvements and modifications also should be regarded as the protection scope of the utility model.
Claims (6)
1. Feed Manufacturing steam condensate recovery system, which is characterized in that including granulator, gas-distributing cylinder, water tank and boiler, divide
Cylinder be connected to by steam pipe a with granulator, is provided with steam-water separator a on steam pipe a, gas-distributing cylinder by condensate pipe a with
Water tank is connected to, and steam-water separator b is provided on condensate pipe a, and water tank is connected by pipeline with boiler, and boiler passes through steam pipe b
It is connected with gas-distributing cylinder, the steam-water separator a is connected to by condensate pipe b with condensate pipe a.
2. Feed Manufacturing steam condensate recovery system according to claim 1, which is characterized in that outside the granulator
Side is provided with air blower, and air blower is connected with jet-stream wind pipe, and the arrival end of jet-stream wind pipe extends to the bottom of granulator.
3. Feed Manufacturing steam condensate recovery system according to claim 2, which is characterized in that the jet-stream wind pipe
Arrival end be provided with jet-stream wind guide plate, jet-stream wind guide plate is set as the guide plate a and guide plate b of two panels tile, leads
The curved wall of plate a and guide plate b are opposite and the certain water conservancy diversion void arrangement in interval forms.
4. Feed Manufacturing steam condensate recovery system according to claim 3, which is characterized in that the jet-stream wind is led
The upper end of plate is provided with gas distributor, gas distributor includes horizontal horizontal disk, disk surrounding and air blower it is interior
Wall is connected, and disc surfaces are uniformly provided with gas port.
5. Feed Manufacturing steam condensate recovery system according to claim 4, which is characterized in that every on the disk
The corresponding position of a gas port is provided with water conservancy diversion paddle, and water conservancy diversion paddle is set as arc paddle blade structure, the free end of water conservancy diversion paddle to
Helically arc-shaped bend extends at disc centre.
6. Feed Manufacturing steam condensate recovery system according to claim 1, which is characterized in that set inside the water tank
It is equipped with floating-ball level switch.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201821653057.1U CN209325761U (en) | 2018-10-12 | 2018-10-12 | Feed Manufacturing steam condensate recovery system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201821653057.1U CN209325761U (en) | 2018-10-12 | 2018-10-12 | Feed Manufacturing steam condensate recovery system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN209325761U true CN209325761U (en) | 2019-08-30 |
Family
ID=67708079
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201821653057.1U Active CN209325761U (en) | 2018-10-12 | 2018-10-12 | Feed Manufacturing steam condensate recovery system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN209325761U (en) |
-
2018
- 2018-10-12 CN CN201821653057.1U patent/CN209325761U/en active Active
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