CN205990408U - A kind of Sugar House crystallizes the heat-insulation system of workshop section's intermediate material - Google Patents
A kind of Sugar House crystallizes the heat-insulation system of workshop section's intermediate material Download PDFInfo
- Publication number
- CN205990408U CN205990408U CN201620661387.XU CN201620661387U CN205990408U CN 205990408 U CN205990408 U CN 205990408U CN 201620661387 U CN201620661387 U CN 201620661387U CN 205990408 U CN205990408 U CN 205990408U
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- China
- Prior art keywords
- heat exchanger
- plate type
- juice
- sugar
- type heat
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Abstract
A kind of Sugar House crystallizes the heat-insulation system of workshop section's intermediate material, including plate type heat exchanger, material storing tank and pump, the soak cycles juice opening of described material storing tank connects through pump and enters juice mouth to plate type heat exchanger, the juice opening of plate type heat exchanger connects and enters juice mouth to the soak cycles of material storing tank, and the air intake of plate type heat exchanger connects two effect juice vapour air supply pipes or triple effect juice vapour air supply pipe to sugar refinery evaporation section.This utility model realize to material be incubated, allow material keep constant temperature, produce on accomplish with take with, it is easy to produce, heated using baffle heater, homogeneous heating, avoid sugar transition, both can reach the temperature of needs with two effect juice vapour, triple effect juice vapour heated material, and be easy to save energy.
Description
Technical field
This utility model is related to Sugar Engineering field, and specifically a kind of Sugar House crystallizes the insulation system of workshop section's intermediate material
System.
Background technology
Cane sugar manufacture is the main mode producing sugar of China, and Caulis Sacchari sinensis candy output exceedes 90% that sugared total amount is produced in the whole nation,
The production carrying out cane sugar manufacture has huge impetus for the economic development of China.First is former, first is washed, second is former and second is washed
Material is the intermediate material of cane sugar manufacture cane sugar boiling and crystal workshop section, and it is former that these intermediate materials are temporarily stored within the former case of first, first tank-washer, second
In case and second tank-washer, then it is re-fed into being processed further in second cream and the third cream crystallizer.In order to above-mentioned intermediate material sends into second cream
With after the third cream crystallizer can rapidly explosive evaporation it is desirable to first is former, first is washed, second is former and second wash storage during keep certain
Temperature.At present, sugar refinery solve method usually directly boiler exhaust steam is passed through in storage tank, exhaust steam be with bagasse heat up water through
The vapour of 120 DEG C about of the temperature producing after steam turbine power generation, although this method can be come with some shortcomings with heated material
Part：(1) directly exhaust steam is passed through in material that material can be caused to be heated is uneven, utilization rate is not high, causes energy waste；(2)
Because boiler exhaust steam temperature is higher, directly heat and during syrup, easily produce caramel；(3) material adopts batch (-type) to heat, temperature wave
Dynamic larger it is impossible to keep material in temperature constant state it is impossible to accomplish with taking with being likely to result in material in heating process violent
Seethe with excitement and diffuse out body feed tank, need the manpower moment to check, manpower consumption is big.(4) with the temperature of the empiric observation material of people,
Stop ventilation before material boiling, manually determine duration of ventilation with micro-judgment, the temperature of material can not be always maintained at perseverance
Temperature, but fluctuated, for the amount of labour also increasing people while producing and control unfavorable.
Content of the invention
This utility model is directed to the deficiencies in the prior art, provides a kind of Sugar House to crystallize the insulation system of workshop section's intermediate material
System, solve traditional direct with exhaust steam, material is carried out easily producing in heating process caramel, vapour heat utilization efficiency not high and
The problem of syrup difficult control of temperature, is favorably improved sugar refinery to the control producing.
To achieve these goals, this utility model employs technical scheme below：
A kind of Sugar House crystallizes the heat-insulation system of workshop section's intermediate material, including plate type heat exchanger, material storing tank and
Pump,
The soak cycles juice opening of described material storing tank connects through pump and enters juice mouth, plate-type heat-exchange to plate type heat exchanger
The juice opening of device connects and enters juice mouth to the soak cycles of material storing tank, and the air intake of plate type heat exchanger connects to sugar refinery evaporator man
Two effect juice vapour air supply pipes of section or triple effect juice vapour air supply pipe.
Described material storing tank is the former case of first, first tank-washer, the former case of second or the second tank-washer of sugar refinery sugar crystallization workshop section.
The honey centrifuge that total material inlet of described material storing tank is former with output first, first is washed, second is former or second is washed is connected, material
Total material outlet of holding vessel connects to second cream or the third cream crystallizer, and the condensation-water drain of plate type heat exchanger connects to condensed water
Tank.
Compared with prior art, the beneficial effect that this utility model possesses：
(1) this utility model realizes material is incubated, and allows material keep constant temperature, accomplishes with taking with being easy on producing
Produce.
(2) prior art exhaust steam, as heater, easily causes and heats uneven, generation caramel.And this utility model
Heated using baffle heater, homogeneous heating, it is to avoid sugar transition.
(3) prior art is used exhaust steam as heating vapour, and exhaust steam temperature is too high, is passed directly into heating heat utilization efficiency in material
Not high, cause the waste of heat, both can reach the temperature of needs with two effect juice vapour, triple effect juice vapour heated material, and be easy to save
The energy.
(4) prior art is directly passed through with exhaust steam and is heated, the difficult control of temperature of material, easily causes material boiling
Diffuse out from body feed tank.And this is heated using new use baffle heater so that material can keep constant temperature, convenient control
The temperature of material.
(5) need not move through the pipeline of complexity in the insulating process of material, increase main equipment it is only necessary to modification several is compared
Short pipeline and increase by one platen type heater, one-time investment low cost can solve the former insulation waiting intermediate material of sugar refinery first
Problem.
Brief description
Fig. 1 is the heat-insulation system that Sugar House described in the utility model crystallizes workshop section's intermediate material.
Specific embodiment
Below by embodiment, the technical solution of the utility model is further elaborated.
Embodiment 1
A kind of Sugar House crystallizes the heat-insulation system of workshop section's intermediate material, including plate type heat exchanger 1, material storing tank 2 with
And pump 4,
The soak cycles juice opening 2a of described material storing tank 2 connects through pump 4 and enters juice mouth 1a to plate type heat exchanger 1,
The juice opening 1b of plate type heat exchanger 1 connects and enters juice mouth 2b, the air intake 1c of plate type heat exchanger 1 to the soak cycles of material storing tank
Connect the two effect juice vapour air supply pipes to sugar refinery evaporation section 3 or triple effect juice vapour air supply pipe.
Described material storing tank is the former case of first, first tank-washer, the former case of second or the second tank-washer of sugar refinery sugar crystallization workshop section.
Total material inlet 2d of described material storing tank 2 is former with output first, first is washed, second is former or second is washed honey centrifuge is connected,
Total material outlet 2c of material storing tank 2 connects to second cream or the third cream crystallizer, and the condensation-water drain 1d of plate type heat exchanger 1 connects
To condensate water pot 5.
Claims (3)
1. a kind of Sugar House crystallizes the heat-insulation system of workshop section's intermediate material it is characterised in that including plate type heat exchanger, material storage
Deposit tank and pump,
The soak cycles juice opening of described material storing tank connects through pump and enters juice mouth to plate type heat exchanger, plate type heat exchanger
Juice opening connects and enters juice mouth to the soak cycles of material storing tank, and the air intake of plate type heat exchanger connects to sugar refinery evaporation section
Two effect juice vapour air supply pipes or triple effect juice vapour air supply pipe.
2. Sugar House as claimed in claim 1 crystallizes the heat-insulation system of workshop section's intermediate material it is characterised in that described material
Holding vessel is the former case of first, first tank-washer, the former case of second or the second tank-washer of sugar refinery sugar crystallization workshop section.
3. Sugar House as claimed in claim 1 crystallizes the heat-insulation system of workshop section's intermediate material it is characterised in that described material
The honey centrifuge that total material inlet of holding vessel is former with output first, first is washed, second is former or second is washed is connected, and total material of material storing tank goes out
Mouth connects to second cream or the third cream crystallizer, and the condensation-water drain of plate type heat exchanger connects to condensate water pot.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620661387.XU CN205990408U (en) | 2016-06-25 | 2016-06-25 | A kind of Sugar House crystallizes the heat-insulation system of workshop section's intermediate material |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620661387.XU CN205990408U (en) | 2016-06-25 | 2016-06-25 | A kind of Sugar House crystallizes the heat-insulation system of workshop section's intermediate material |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205990408U true CN205990408U (en) | 2017-03-01 |
Family
ID=58102356
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201620661387.XU Expired - Fee Related CN205990408U (en) | 2016-06-25 | 2016-06-25 | A kind of Sugar House crystallizes the heat-insulation system of workshop section's intermediate material |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205990408U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110205410A (en) * | 2019-05-31 | 2019-09-06 | 广西吉然科技有限公司 | A kind of novel molasses dilution technique |
-
2016
- 2016-06-25 CN CN201620661387.XU patent/CN205990408U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110205410A (en) * | 2019-05-31 | 2019-09-06 | 广西吉然科技有限公司 | A kind of novel molasses dilution technique |
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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 |
Granted publication date: 20170301 Termination date: 20170625 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |