CN209302558U - A kind of raw sugar syrup inverting equipment - Google Patents
A kind of raw sugar syrup inverting equipment Download PDFInfo
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- CN209302558U CN209302558U CN201822101628.7U CN201822101628U CN209302558U CN 209302558 U CN209302558 U CN 209302558U CN 201822101628 U CN201822101628 U CN 201822101628U CN 209302558 U CN209302558 U CN 209302558U
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- syrup
- heat exchanger
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- raw sugar
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Abstract
The utility model discloses a kind of raw sugar syrup inverting equipments, its including sugar slot, buffer tank and condensate pump, the outer wall for changing sugared slot is equipped with vapor heat exchanger, the gas outlet of vapor heat exchanger and the inlet communication of buffer tank, the outlet of buffer tank and the inlet communication of condensate pump, the outlet of condensate pump are connected to boiler water inlet pipe.Advantage: heat exchange enquirement is carried out to change syrup outside the sugared slot of change using vapor heat exchanger, so that each section syrup asks uniform raising, promotionization syrup heating rate, it is that raw sugar sufficiently dissolves, improve solution rate, the solution rate of raw sugar can be further speeded up changing setting agitating shaft and stirring blade in sugared slot, and ensures the uniformity of temperature raising；Steam can be kept apart simultaneously with syrup is changed, steam condensate is avoided to mix with syrup is changed, and then ensured raw sugar and change the accurate proportion of syrup；Meanwhile the higher boiler that is sent directly into of vapor (steam) temperature after heat exchange is recycled, and boiler energy consumption can be reduced while reducing boiler feed water, and then reduce production cost.
Description
Technical field:
The utility model relates to a kind of syrup inverting equipments, relate in particular to a kind of raw sugar syrup inverting equipment.
Background technique:
Raw sugar is to be process sugar cane crushing, peace and quiet, Zhu refining, and granularity is larger, sugar is excessively high, cannot directly eat
With, be sugar refinery reprocessing raw material sugar；Sugar refinery needs to wash raw sugar progress sugar, honey, secondary screening, recrystallization etc.
Edible granulated sugar is obtained after reason.Wherein, sugar melting process is to recycle heater to add pure water in the sugared slot of raw sugar additionization
Heat, as syrup and raw sugar hybridization sugar is changed, is passed through 140 ° of steam into the sugared slot of feedingization after 80 ° into the sugared slot of change again later
Carry out temperature raising heating；But it in the sugared heating process of thisization, is mixed in steam being passed directly into syrup with raw sugar, will cause office
Portion's syrup temperature increases, but whole heating rate is slow, and raw sugar dissolution is insufficient, and the condensed water of steam generation directly dissolves
In changing syrup, influences raw sugar and change the proportion of syrup, the precision of influence sugar, meanwhile, the condensed water of steam generation directly quilt
Change syrup to take away, steam consumption is big, causes steam boiler water and energy consumption to increase, high production cost.
Utility model content:
The purpose of this utility model is to provide a kind of raw sugar syrup inverting equipments that solution rate is fast.
The utility model is implemented by following technical solution: a kind of raw sugar syrup inverting equipment comprising changes sugared slot, buffer tank and coagulates
Pump is born water, is communicated with water inlet in one end of the sugared slot of describedization, is communicated with water outlet in the other end of the sugared slot of describedization；Described
The outer wall for changing sugared slot is equipped with vapor heat exchanger, and the inlet communication of the gas outlet of the vapor heat exchanger and the buffer tank is described
The outlet of buffer tank and the inlet communication of the condensate pump, the outlet of the condensate pump is connected to boiler water inlet pipe.
Further, it is equipped with horizontally disposed agitating shaft in the middle part rotation of the sugared slot of describedization, on the agitating shaft
It is even to be fixed with stirring blade；The motor with agitating shaft transmission connection is provided with outside the sugared slot of describedization.
Further, each stirring blade is arranged in the shape of a spiral in the stirring axial length, and the stirring blade
Direction of rotation is opposite with the sugared slot internalization flow direction of syrup is changed.
Further, it is fixed in the sugared slot inner vertical of describedization and overflows what the water inlet and the water outlet separated
Flowing plate.
Further, the being provided with syrup heat exchanger between the buffer tank and the gas outlet of the vapor heat exchanger,
The first entrance and first outlet of describedization syrup heat exchanger respectively with the gas outlet of the vapor heat exchanger and the buffer tank
Inlet communication, second medium entrance and the second medium outlet of describedization syrup respectively with change syrup water source and the water inlet
Connection.
The advantages of the utility model: carrying out heat exchange enquirement to change syrup outside the sugared slot of change using vapor heat exchanger, so that
Each section syrup asks uniform raising, and promotionization syrup heating rate is that raw sugar sufficiently dissolves, and improves solution rate, is changing sugar
Setting agitating shaft and stirring blade can further speed up the solution rate of raw sugar in slot, and ensure the uniformity of temperature raising；It simultaneously can
Steam is kept apart with syrup is changed, steam condensate is avoided to mix with syrup is changed, and then ensures raw sugar and changes accurately matching for syrup
Than；Meanwhile the higher boiler that is sent directly into of vapor (steam) temperature after heat exchange is recycled, and can be reduced while reducing boiler feed water
Boiler energy consumption, and then reduce production cost.
Detailed description of the invention:
Fig. 1 is the overall structure diagram of embodiment 1.
Fig. 2 is the overall structure diagram of embodiment 2.
Change sugared slot 1, buffer tank 2, condensate pump 3, water inlet 4, water outlet 5, vapor heat exchanger 6, boiler 7, agitating shaft 8,
Stirring blade 9, changes syrup heat exchanger 11, overflow plate 12 at motor 10.
Specific embodiment:
Embodiment 1: as shown in Figure 1, a kind of raw sugar syrup inverting equipment comprising change sugared slot 1, buffer tank 2 and condensate pump 3,
It is communicated with water inlet 4 in the one end for changing sugared slot 1, is communicated with water outlet 5 in the other end for changing sugared slot 1；Change syrup to send through water inlet 4
Entering sugar slot 1, the syrup after changing sugar are sent out by water outlet 5；It is fixed with changing sugared 1 inner vertical of slot by water inlet 4 and water outlet 5
Raw sugar is added in the change sugar slot 1 of 4 side of water inlet by the overflow plate 12 separated, is made it and is changed the present water inlet 4 one of syrup
Side mixing, overflows in the change sugar slot 1 of 5 side of water outlet later through overflow plate 12, again when the mixing of extensionization syrup and raw sugar
Between.
It is equipped with vapor heat exchanger 6 in the outer wall for changing sugared slot 1, the gas outlet of vapor heat exchanger 6 and the import of buffer tank 2 connect
Logical, the outlet of buffer tank 2 and the inlet communication of condensate pump 3, the outlet of condensate pump 3 is connected to 7 water inlet pipe of boiler；Steam into
Heating temperature raising is carried out to the change syrup changed in sugared slot 1 after entering vapor heat exchanger 6, the steam after heat exchange is discharged by vapor heat exchanger 6
Enter buffer tank 2 afterwards and carry out caching and condense into condensed water, after be pumped into boiler 7 through condensate pump 3 and heated again, it is real
Existing steam condensate recycles；
It is equipped with horizontally disposed agitating shaft 8 in the middle part rotation for changing sugared slot 1, is uniformly fixed with paddle on agitating shaft 8
Piece 9；The motor 10 being sequentially connected with agitating shaft 8 is provided with outside sugared slot 1 changing；Motor 10 drives agitating shaft 8 to rotate, then band
The change syrup and raw sugar changed in sugared slot 1 is sufficiently stirred in the dynamic rotation of stirring blade 9 so that change syrup mixing with realize
Accelerate the solution rate of raw sugar while uniform temperature raising.
Operation instruction: firstly, raw sugar is added in the change sugar slot 1 of 4 side of water inlet, and pass through 4 additionization of water inlet
Syrup；Later, start motor 10, and be passed through steam into vapor heat exchanger 6, motor 10 drives 9 agitationization syrup of stirring blade
While by steam temperature raising so that raw sugar and change syrup and be sufficiently mixed into syrup, after after 12 overflow of overflow plate by being discharged
Mouth 5 is discharged；Steam after heat exchange, which then enters after buffer tank 2 condenses to be pumped into boiler 7 by condensate pump 2, to be recycled.
Embodiment 2: as shown in Fig. 2, its overall structure is same as Example 1, the difference is that, each stirring blade 9
Arranged in the shape of a spiral in the length of agitating shaft 8, and the direction of rotation of stirring blade 9 and change sugared slot 1 be internalized by syrup flow direction on the contrary,
By the reversed agitationization syrup of stirring blade 9 and raw sugar, it is sufficiently mixed so that changing syrup with raw sugar, reinforces solute effect；
The being provided with syrup heat exchanger 11 between buffer tank 2 and the gas outlet of vapor heat exchanger 6 changes syrup heat exchanger 11
First entrance and the first outlet inlet communication with the gas outlet of vapor heat exchanger 6 and buffer tank 2 respectively, change the second of syrup
Medium inlet and second medium outlet are connected to change syrup water source and water inlet 4 respectively；The initial temperature for changing syrup is 80 °, is steamed
The initial temperature of vapour is 140 °, and the vapor (steam) temperature after heat exchange is up to 120 °, by the change before the steam and the sugared slot 1 of entranceization after heat exchange
It in syrup feedingization syrup heat exchanger 11, is preheated using the steam after heat exchange to syrup is changed, directly raising entranceization sugar
The temperature of the change syrup of slot 1, further speeds up solution rate and heating up speed.
The above is only the preferred embodiment of the utility model only, is not intended to limit the utility model, all at this
Within the spirit and principle of utility model, any modification, equivalent replacement, improvement and so on should be included in the utility model
Protection scope within.
Claims (6)
1. a kind of raw sugar syrup inverting equipment, which is characterized in that its including sugar slot, buffer tank and condensate pump, in the sugared slot of describedization
One end be communicated with water inlet, be communicated with water outlet in the other end of the sugared slot of describedization；It is equipped with and steams in the outer wall of the sugared slot of describedization
Vapour heat exchanger, the inlet communication of the gas outlet of the vapor heat exchanger and the buffer tank, the outlet of the buffer tank with it is described
The outlet of the inlet communication of condensate pump, the condensate pump is connected to boiler water inlet pipe.
2. a kind of raw sugar syrup inverting equipment according to claim 1, which is characterized in that set in the middle part rotation of the sugared slot of describedization
There is horizontally disposed agitating shaft, is uniformly fixed with stirring blade on the agitating shaft；Be provided with outside the sugared slot of describedization with
The motor of the agitating shaft transmission connection.
3. a kind of raw sugar syrup inverting equipment according to claim 2, which is characterized in that each stirring blade is stirred described
It mixes axial length to arrange in the shape of a spiral, and the flow direction phase of the direction of rotation of the stirring blade and the sugared slot internalization syrup of describedization
Instead.
4. a kind of raw sugar syrup inverting equipment according to any one of claims 1 to 3, which is characterized in that inside the sugared slot of describedization
It is vertically fixed the overflow plate for separating the water inlet and the water outlet.
5. a kind of raw sugar syrup inverting equipment according to any one of claims 1 to 3, which is characterized in that in the buffer tank and institute
Being provided with syrup heat exchanger between the gas outlet of vapor heat exchanger is stated, the first entrance of describedization syrup heat exchanger and first go out
The mouth inlet communication with the gas outlet of the vapor heat exchanger and the buffer tank respectively, the second medium entrance of describedization syrup
It is connected to respectively with change syrup water source and the water inlet with second medium outlet.
6. a kind of raw sugar syrup inverting equipment according to claim 4, which is characterized in that changed in the buffer tank and the steam
Being provided with syrup heat exchanger between the gas outlet of hot device, the first entrance and first outlet of describedization syrup heat exchanger respectively with
The inlet communication of the gas outlet of the vapor heat exchanger and the buffer tank, the second medium entrance of describedization syrup and second are situated between
Matter outlet is connected to change syrup water source and the water inlet respectively.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201822101628.7U CN209302558U (en) | 2018-12-13 | 2018-12-13 | A kind of raw sugar syrup inverting equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201822101628.7U CN209302558U (en) | 2018-12-13 | 2018-12-13 | A kind of raw sugar syrup inverting equipment |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN209302558U true CN209302558U (en) | 2019-08-27 |
Family
ID=67676980
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201822101628.7U Active CN209302558U (en) | 2018-12-13 | 2018-12-13 | A kind of raw sugar syrup inverting equipment |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN209302558U (en) |
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2018
- 2018-12-13 CN CN201822101628.7U patent/CN209302558U/en active Active
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