CN207462696U - A kind of evaporator control system - Google Patents
A kind of evaporator control system Download PDFInfo
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- CN207462696U CN207462696U CN201721303941.8U CN201721303941U CN207462696U CN 207462696 U CN207462696 U CN 207462696U CN 201721303941 U CN201721303941 U CN 201721303941U CN 207462696 U CN207462696 U CN 207462696U
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- evaporator
- control system
- discharging pump
- discharging
- steam
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Abstract
The utility model discloses a kind of evaporator control systems, at the temperature of setting and traffic conditions, pressure is directly proportional to viscosity, there are specific functional relations between viscosity and the concentration of gelatin solution, the pressure stability of gelatin solution that evaporator control system provided by the utility model is flowed out by adjustable second discharging pump of flow from the second discharging pump is within the scope of one, the gelatin solution for so also allowing for different quality is finally similar in dry link, convenient for subsequent drying process；In addition, the evaporation that heats up to the gradient type of gelatin solution is also realized, and sediment in gelatin solution and suspended matter are efficiently separated by the realization of same cyclone hydraulic separators by the syntagmatic between evaporator.
Description
Technical field
The utility model belongs to manufacturing of gelatin equipment technical field, more particularly, to a kind of evaporator control system.
Background technology
Gelatin is a kind of high-molecular compound, is widely used in food, medicine, chemical industry, weaving, printing, papermaking, hardware, family
In numerous industries such as tool, photosensitive material.The primary raw material for producing gelatin is the cladding or aggregate of the animals such as pig, ox, sheep.
Evaporator is the important equipment for producing gelatin, is played an important role in manufacturing of gelatin, therefore, for different groups
The control of the evaporator of conjunction is also particularly important.
Utility model content
The purpose of this utility model is that for the deficiencies in the prior art, a kind of evaporator control system is provided.
For this purpose, the above-mentioned purpose of the utility model is achieved through the following technical solutions：
A kind of evaporator control system, the evaporator control system include multiple evaporators and are connected with evaporator
Cyclone hydraulic separators, the feed inlet of the cyclone hydraulic separators are connected with the discharge port of each evaporator, the cyclone hydraulic separators
Discharge port is connected with the feed inlet of non-first evaporator, and the circulating and evaporating that evaporator combinations are formed with this controls；The rotation
The corresponding discharge nozzle of the discharge port of liquid/gas separator is equipped with the first discharging pump, the downstream setting discharging branch of first discharging pump
Pipe and loop branch pipe, the discharging branch pipe are equipped with the second discharging pump, and second discharging pump is pumped for flow discharge adjustable, institute
The feed inlet that loop branch pipe is stated with non-first evaporator is connected, loop exit and the loop branch pipe phase of second discharging pump
Connection and the feed inlet for accessing to non-first evaporator.
The utility model provides a kind of evaporator control system, at the temperature of setting and traffic conditions, pressure and viscosity
Directly proportional, there are specific functional relation, evaporator controls provided by the utility model between viscosity and the concentration of gelatin solution
System processed is existed by the pressure stability of gelatin solution that adjustable second discharging pump of flow is flowed out from the second discharging pump
Within the scope of one, then the gelatin solution for also allowing for different quality is finally similar in dry link, convenient for subsequent dry
Drying process；In addition, the evaporation that heats up to the gradient type of gelatin solution is also realized, and lead to by the syntagmatic between evaporator
Same cyclone hydraulic separators realization is crossed to efficiently separate sediment in gelatin solution and suspended matter.
While using above-mentioned technical proposal, the utility model can also be used or be combined using further below
Technical solution：
Preferably, the steam (vapor) outlet of next stage evaporator is connected to the steam inlet of upper level evaporator.The utility model
By the way that the steam (vapor) outlet of next stage evaporator to be connected to the steam inlet of upper level evaporator, because in next stage evaporator
Temperature is higher than the temperature in upper level evaporator, therefore, by the connection of such mode, so as to make full use of next stage evaporator
The residual heat of the indirect steam of discharge, and by the residual heat come the gelatin solution in upper level evaporator that heats up, thus
Realize energy-saving and environment-friendly requirement.
Preferably, the steam inlet of afterbody evaporator is connected with extraneous steam generation device.
Preferably, the steam (vapor) outlet of first evaporator is connected to the overflow pipe of cyclone hydraulic separators.The utility model is by
The steam (vapor) outlet of level-one evaporator is connected to the overflow pipe of cyclone hydraulic separators, can will be arranged in indirect steam and cyclone hydraulic separators
It is discharged after the overflowing liquid mixing gone out.
Preferably, first discharging pump is unidirectional electromagnetic pump.
Preferably, second discharging pump is that unidirectional electromagnetic pump is adjusted.
Description of the drawings
Fig. 1 is a kind of schematic diagram of evaporator control system provided by the utility model；
In figure：11- first evaporators；The discharge port of 111- first evaporators；The charging of 112- first evaporators
Mouthful；The steam (vapor) outlet of 113- first evaporators；The steam inlet of 114- first evaporators；12- second level evaporator；121-
The discharge port of second level evaporator；The feed inlet of 122- second level evaporator；The steam (vapor) outlet of 123- second level evaporator；124-
The steam inlet of second level evaporator；2- cyclone hydraulic separators；The feed inlet of 21- cyclone hydraulic separators；The discharging of 22- cyclone hydraulic separators
Mouthful；The overflow pipe of 23- cyclone hydraulic separators；31- discharge nozzles；32- discharging branch pipes；33- loop branch pipes；The first discharging pumps of 41-；42-
Second discharging pump.
Specific embodiment
The utility model is described in further detail with reference to the drawings and specific embodiments.
A kind of evaporator control system, including first evaporator 11, second level evaporator 12 and with cyclone hydraulic separators 2,
The feed inlet 21 of cyclone hydraulic separators 2 is connected respectively with the discharge port of double effect evaporator 111,121, the discharging of cyclone hydraulic separators 2
Mouth 22 is connected with the feed inlet 122 of second level evaporator 12, and the feed inlet 112 of first evaporator 11 is connected with upstream device
Lead to, and the circulating and evaporating control of double effect evaporator combination is formed with this；Discharge nozzle corresponding to the discharge port 22 of cyclone hydraulic separators 2
31 are equipped with the first discharging pump 41, the downstream setting discharging branch pipe 32 and circulation pipe 33 of the first discharging pump 41, and the branch pipe 32 that discharges
It is connected with circulation pipe 33 with the first discharging pump 41, discharging branch pipe 32 is equipped with the second discharging pump 42, and the second discharging pump 42 is
Flow discharge adjustable pumps, and the loop exit of the second discharging pump 42, which is connected with loop branch pipe 33 and is passed through to the second level, to be evaporated
The feed inlet 122 of device 12.
At the temperature of setting and traffic conditions, pressure is directly proportional to viscosity, is deposited between viscosity and the concentration of gelatin solution
In specific functional relation, evaporator control system provided by the utility model is made by adjustable second discharging pump of flow
The pressure stability of gelatin solution flowed out from the second discharging pump is obtained within the scope of one, then also allow for the bright of different quality
Sol solution is finally similar in dry link, convenient for subsequent drying process；In addition, it is also closed by the combination between evaporator
System realizes the evaporation that heats up to the gradient type of gelatin solution, and is realized by same cyclone hydraulic separators to sinking in gelatin solution
Starch and suspended matter efficiently separate.
The steam (vapor) outlet 123 of second level evaporator 12 is connected to the steam inlet 114 of first evaporator 11.By by
The steam (vapor) outlet of secondary evaporimeter is connected to the steam inlet of first evaporator, because the temperature in the evaporator of the second level is higher than
Temperature in first evaporator, therefore, by the connection of such mode, so as to make full use of the two of second level evaporator discharge
The residual heat of secondary steam, and by the residual heat come the gelatin solution in first evaporator that heats up, so as to fulfill energy saving
The requirement of environmental protection.
The steam inlet 124 of second level evaporator 12 is connected with extraneous steam generation device.
The steam (vapor) outlet 113 of first evaporator 11 is connected to the overflow pipe 23 of cyclone hydraulic separators 2.By first evaporator
Steam (vapor) outlet be connected to the overflow pipe of cyclone hydraulic separators, can be by the overflowing liquid discharged in indirect steam and cyclone hydraulic separators
It is discharged after mixing.
First discharging pump 41 is unidirectional electromagnetic pump.
Second discharging pump 42 is that unidirectional electromagnetic pump is adjusted.
Show to be double effect evaporator in the present embodiment, certainly in other embodiments, can also use more than two-stage
Evaporator, and can realize that the combination of evaporator controls using the connection relation similar to the present embodiment, and these are directed to
The improvement and deformation of the present embodiment are in the scope of protection of the utility model.
Above-mentioned specific embodiment is used for illustrating the preferred embodiment of the utility model, only the utility model, and
It is not that the utility model is limited, it is new to this practicality in the spirit and scope of the claims of the utility model
Any modification, equivalent substitution, improvement and etc. that type is made, both fall within the scope of protection of the utility model.
Claims (6)
1. a kind of evaporator control system, which is characterized in that the evaporator control system include multiple evaporators and with evaporation
The cyclone hydraulic separators that device is connected, the feed inlet of the cyclone hydraulic separators are connected with the discharge port of each evaporator, the rotation
The discharge port of liquid/gas separator is connected with the feed inlet of non-first evaporator, and the circulating and evaporating control of evaporator combinations is formed with this
System；The corresponding discharge nozzle of the discharge port of the cyclone hydraulic separators is equipped with the first discharging pump, the downstream of first discharging pump
Setting discharging branch pipe and loop branch pipe, the discharging branch pipe are equipped with the second discharging pump, and second discharging pump is adjustable for flow
Discharging pump is saved, the loop branch pipe is connected with the feed inlet of non-first evaporator, the loop exit of second discharging pump
It is connected and accesses to the feed inlet of non-first evaporator with loop branch pipe.
2. evaporator control system according to claim 1, which is characterized in that the steam (vapor) outlet connection of next stage evaporator
To the steam inlet of upper level evaporator.
3. evaporator control system according to claim 1, which is characterized in that the steam inlet of afterbody evaporator with
Extraneous steam generation device is connected.
4. according to the evaporator control system described in any one in claim 1-3, which is characterized in that first evaporator
Steam (vapor) outlet is connected to the overflow pipe of cyclone hydraulic separators.
5. evaporator control system according to claim 1, which is characterized in that first discharging pump is unidirectional electromagnetism
Pump.
6. evaporator control system according to claim 1, which is characterized in that second discharging pump is adjustable unidirectional
Electromagnetic pump.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721303941.8U CN207462696U (en) | 2017-10-11 | 2017-10-11 | A kind of evaporator control system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721303941.8U CN207462696U (en) | 2017-10-11 | 2017-10-11 | A kind of evaporator control system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN207462696U true CN207462696U (en) | 2018-06-08 |
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ID=62266657
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201721303941.8U Active CN207462696U (en) | 2017-10-11 | 2017-10-11 | A kind of evaporator control system |
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| CN (1) | CN207462696U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN115228108A (en) * | 2022-06-07 | 2022-10-25 | 珠海市裕洲环保科技有限公司 | Dilute sulfuric acid recovery device |
-
2017
- 2017-10-11 CN CN201721303941.8U patent/CN207462696U/en active Active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN115228108A (en) * | 2022-06-07 | 2022-10-25 | 珠海市裕洲环保科技有限公司 | Dilute sulfuric acid recovery device |
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