CN207132755U - A kind of albumin milk liquefaction heat-exchanger rig - Google Patents
A kind of albumin milk liquefaction heat-exchanger rig Download PDFInfo
- Publication number
- CN207132755U CN207132755U CN201720849281.7U CN201720849281U CN207132755U CN 207132755 U CN207132755 U CN 207132755U CN 201720849281 U CN201720849281 U CN 201720849281U CN 207132755 U CN207132755 U CN 207132755U
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- CN
- China
- Prior art keywords
- heat
- exchanger rig
- condensed water
- water
- exhaust outlet
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Fee Related
Links
- 235000013336 milk Nutrition 0.000 title claims abstract description 31
- 239000008267 milk Substances 0.000 title claims abstract description 31
- 210000004080 milk Anatomy 0.000 title claims abstract description 31
- 102000009027 Albumins Human genes 0.000 title claims abstract description 19
- 108010088751 Albumins Proteins 0.000 title claims abstract description 19
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 86
- 239000000463 material Substances 0.000 claims abstract description 13
- 230000006835 compression Effects 0.000 claims abstract description 9
- 238000007906 compression Methods 0.000 claims abstract description 9
- 125000004122 cyclic group Chemical group 0.000 claims abstract description 6
- 229920002472 Starch Polymers 0.000 claims description 12
- 235000019698 starch Nutrition 0.000 claims description 12
- 239000008107 starch Substances 0.000 claims description 12
- 239000000376 reactant Substances 0.000 claims description 10
- 238000010612 desalination reaction Methods 0.000 claims description 6
- 230000006698 induction Effects 0.000 claims description 6
- 238000009434 installation Methods 0.000 claims description 6
- 102000004195 Isomerases Human genes 0.000 claims description 3
- 108090000769 Isomerases Proteins 0.000 claims description 3
- 230000036571 hydration Effects 0.000 claims description 3
- 238000006703 hydration reaction Methods 0.000 claims description 3
- 238000002360 preparation method Methods 0.000 claims description 3
- 101100194816 Caenorhabditis elegans rig-3 gene Proteins 0.000 claims 1
- 101100194817 Caenorhabditis elegans rig-6 gene Proteins 0.000 claims 1
- 101150006257 rig-4 gene Proteins 0.000 claims 1
- 102000004169 proteins and genes Human genes 0.000 abstract description 9
- 108090000623 proteins and genes Proteins 0.000 abstract description 9
- 238000000034 method Methods 0.000 abstract description 6
- 238000010438 heat treatment Methods 0.000 abstract description 3
- 230000033228 biological regulation Effects 0.000 abstract description 2
- 238000009833 condensation Methods 0.000 abstract description 2
- 230000005494 condensation Effects 0.000 abstract description 2
- 238000001816 cooling Methods 0.000 abstract description 2
- 238000004519 manufacturing process Methods 0.000 description 5
- 238000004140 cleaning Methods 0.000 description 2
- 239000000843 powder Substances 0.000 description 2
- 102000004190 Enzymes Human genes 0.000 description 1
- 108090000790 Enzymes Proteins 0.000 description 1
- 238000007792 addition Methods 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000002347 injection Methods 0.000 description 1
- 239000007924 injection Substances 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 239000000243 solution Substances 0.000 description 1
- 238000006467 substitution reaction Methods 0.000 description 1
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- Dairy Products (AREA)
Abstract
It the utility model is related to a kind of albumin milk liquefaction heat-exchanger rig, the device allows the flow of protein feed to be adjusted by control device, feed pump is provided with Frequency Converter Control rotating speed, in real time flow control is realized according to setting requirements, the temperature of the first temperature sensing device can be configured after determining flow, compression pump on first condensed water exhaust outlet can adjust condensation flow speed according to the temperature and flow of setting, the condensed water of residual flow enters next procedure after being cooled by the cyclic water tank on the second condensed water exhaust outlet, material and condensate temperature after heat-exchanger rig exchanges heat reach technological requirement, whole process realizes automation regulation.Bi-directional energy-saving will be realized in the heating process of the UTILIZATION OF VESIDUAL HEAT IN of condensed water to Protein material, not only save the energy resource consumption of Protein material heating, while save the energy resource consumption of condensed water cooling, it is simple to operate.
Description
Technical field
Albumen powder production technical field is the utility model is related to, the device produced in particular for albumen powder, specially one
Kind albumin milk liquefaction heat-exchanger rig.
Background technology
During albumin milk liquefaction, after the completion of reacting in desalination water pot, can discharge 45 degrees centigrades protein feed and
The condensed water of 80 degrees centigrades, in traditional handicraft, the protein feed of 45 degrees centigrades needs to be heated to 62 degrees centigrades
Lower road saccharification process could be entered, and the condensed water of 80 degrees centigrades needs to cool to 62 degrees centigrades by cyclic water tank
It could be used for next procedure, the temperature-rise period of protein feed and condensed water temperature-fall period first can all consume big energy, secondly
The condensed water of 80 degrees centigrades is difficult to drop to 62 degrees Celsius when circulating water temperature easily reaches 30 degrees Celsius, and to plate-type heat-exchange
Device circulating water channel incrustation scale blocks seriously, needs shutdown to carry out opening dismounting cleaning in each season, has a strong impact on the suitable of production
Profit operation is, it is necessary to often take cleaning apart and need within every 2 years to change whole plate, increase production cost；It is Celsius higher than 62
The condensed water of degree can cause to damage to equipment, reduce service life of equipment；Urgent need to resolve energy expenditure is big and equipment excess load is transported
Turn problem.
Utility model content
The utility model aims to overcome that the deficiency of the above, there is provided a kind of albumin milk liquefaction heat exchange dress of convenient use
Put, save energy expenditure, improve service life of equipment.
The utility model purpose is achieved through the following technical solutions such a albumin milk liquefaction heat-exchanger rig, including reactant plus
Enter device（1）, feed arrangement（2）, vapor can（3）, hot desalinized water tank（4）, reactant adding apparatus（1）Enter by first and manage
（7）With hot desalinized water tank（4）Connection, feed arrangement（2）And vapor can（3）Enter by second and manage（8）With hot desalinized water tank（4）
Connection；Hot desalinized water tank（4）Provided with discharge nozzle（5）, condensed water discharge pipe（6）, the discharge nozzle（5）, condensed water discharge pipe（6）
Respectively with heat-exchanger rig（9）Charging aperture（9-1）And water inlet（9-2）Connection.
As preferred：Condensed water discharge pipe（6）Including the first condensed water exhaust outlet（6-1）Branch is discharged with the second condensed water
Pipe（6-2）, the first condensed water exhaust outlet（6-1）With heat-exchanger rig（9）Water inlet（9-2）Connection, the discharge of the second condensed water
Branch pipe（6-2）With cyclic water tank（10）Connection, the first condensed water exhaust outlet（6-1）It is provided with compression pump（11）And first flow
Meter（12）, compression pump（11）And first flowmeter（12）With control device（13）Connection.
As preferred：Charging aperture（9-1）It is provided with feed pump（14）And second flowmeter（15）, feed pump（14）With second
Flowmeter（15）Respectively with control device（13）Connection.
As preferred：Heat-exchanger rig（9）It is provided with heat-exchanger rig discharge nozzle（9-3）And outlet pipe（9-4）, the heat exchange dress
Put discharge nozzle（9-3）And outlet pipe（9-4）It is respectively equipped with the first temperature sensing device（16）With second temperature induction installation（17）,
First temperature sensing device（16）With second temperature induction installation（17）Respectively with control device（13）Connection.
As preferred：Reactant adding apparatus（1）Including cold desalination water pot（1-1）, starch milk preparation tank（1-2）, injection
Head tank（1-3）, isomerase hydration tank（1-4）, starch milk holding vessel（1-5）, finished product evaporator（1-6）, starch milk thickens water
Tank（1-7）.
As preferred：Heat-exchanger rig（9）Positive U-shaped and the inverted U-shaped material passing tube ganged up（9-5）Be wrapped in material passing tube（9-5）
On water service pipe（9-6）.
The utility model albumin milk liquefaction heat-exchanger rig realizes automated production, and the flow of protein feed can pass through control
Device is adjusted, and feed pump is provided with Frequency Converter Control rotating speed, realizes flow control according to setting requirements in real time, determines stream
The temperature of the first temperature sensing device can be configured after amount, the compression pump meeting basis on the first condensed water exhaust outlet is set
Temperature and flow the adjustment condensation flow speed put, the condensed water of residual flow pass through the circulation on the second condensed water exhaust outlet
Water tank enters next procedure after being cooled, and the material and condensate temperature after heat-exchanger rig exchanges heat reach technological requirement,
Whole process is realized by control device, realizes automation regulation.
The utility model has advantages below：The utility model is by the UTILIZATION OF VESIDUAL HEAT IN of condensed water to the heated of Protein material
Bi-directional energy-saving is realized in journey, not only saves the energy resource consumption of Protein material heating, while saves the energy of condensed water cooling
Source consumes；Automated condtrol is realized, leads to ancient control device control discharging flow and temperature, water flow and temperature, operation letter
Folk prescription is just.
Brief description of the drawings
Fig. 1 is the structural representation of this albumin milk liquefaction heat-exchanger rig.
In figure：1:Reactant adding apparatus, 2:Feed arrangement, 3:Vapor can, 4:Hot desalinized water tank, 5:Discharge nozzle,
6:Condensed water discharge pipe, 7:First entrance pipe, 8:Second entrance pipe, 9：Heat-exchanger rig, 10：Cyclic water tank, 11：Compression pump,
12：First flowmeter, 13：Control device, 14：Feed pump, 15：Second flowmeter, 16：First temperature sensing device, 17：Second
Temperature sensing device, 1-1：Cold desalination water pot, 1-2：Starch milk prepares tank, 1-3:It is injected into batch can, 1-4:Isomerase aquation
Tank, 1-5:Starch milk holding vessel, 1-6:Finished product evaporator, 1-7：Starch milk thickens water pot, 6-1：First condensed water discharge branch
Pipe, 6-2：Second condensed water exhaust outlet, 9-1：Charging aperture, 9-2：Water inlet, 9-3：Heat-exchanger rig discharge nozzle, 9-4：Water outlet
Pipe, 9-5：Material passing tube, 9-6：Water service pipe.
Embodiment
In order to deepen to understanding of the present utility model, the utility model albumin milk is liquefied below in conjunction with example and accompanying drawing
Heat-exchanger rig makees further detailed art, and the embodiment is only used for explaining the utility model, does not form and protect model to the utility model
The restriction enclosed.
As Fig. 1 shows a kind of embodiment of albumin milk liquefaction heat-exchanger rig, a kind of albumin milk liquefaction heat-exchanger rig, bag
Include reactant adding apparatus（1）, feed arrangement（2）, vapor can（3）, hot desalinized water tank（4）, reactant adding apparatus（1）Pass through
First enters pipe（7）With hot desalinized water tank（4）Connection, feed arrangement（2）And vapor can（3）Enter by second and manage（8）With heat
Desalination water pot（4）Connection；Hot desalinized water tank（4）Provided with discharge nozzle（5）, condensed water discharge pipe（6）, discharge nozzle（5）, condensed water row
Outlet pipe（6）Respectively with heat-exchanger rig（9）Charging aperture（9-1）And water inlet（9-2）Connection；Condensed water discharge pipe（6）Including
One condensed water exhaust outlet（6-1）With the second condensed water exhaust outlet（6-2）, the first condensed water exhaust outlet（6-1）With heat exchange
Device（9）Water inlet（9-2）Connection, the second condensed water exhaust outlet（6-2）With cyclic water tank（10）Connection, the first condensed water
Exhaust outlet（6-1）It is provided with compression pump（11）And first flowmeter（12）, compression pump（11）And first flowmeter（12）With control
Device processed（13）Connection；Charging aperture（9-1）It is provided with feed pump（14）And second flowmeter（15）, feed pump（14）And second
Gauge（15）Respectively with control device（13）Connection.Heat-exchanger rig（9）It is provided with heat-exchanger rig discharge nozzle（9-3）And outlet pipe
（9-4）, heat-exchanger rig discharge nozzle（9-3）And outlet pipe（9-4）It is respectively equipped with the first temperature sensing device（16）And second temperature
Induction installation（17）, the first temperature sensing device（16）With second temperature induction installation（17）Respectively with control device（13）Even
Connect；Reactant adding apparatus（1）Including cold desalination water pot（1-1）, starch milk preparation tank（1-2）, it is injected into batch can（1-3）, it is different
Structure enzyme hydration tank（1-4）, starch milk holding vessel（1-5）, finished product evaporator（1-6）, starch milk thickens water pot（1-7）；Heat exchange dress
Put（9）Positive U-shaped and the inverted U-shaped material passing tube ganged up（9-5）Be wrapped in material passing tube（9-5）On water service pipe（9-6）.
In summary, new albumin milk liquefaction heat-exchanger rig uses, easy for operation, has saved the energy, has reduced factory
Production cost.
It is to be also not limited to the example above, this skill to limitation of the present utility model, the utility model that described above, which is not,
The variations, modifications, additions or substitutions that the those of ordinary skill in art field is made in essential scope of the present utility model, also should
Belong to the scope of protection of the utility model.
Claims (6)
- The heat-exchanger rig 1. a kind of albumin milk liquefies, it is characterised in that including：Reactant adding apparatus（1）, feed arrangement（2）, steam Vapour tank（3）, hot desalinized water tank（4）, the reactant adding apparatus（1）Enter by first and manage（7）With hot desalinized water tank（4）Even Connect, the feed arrangement（2）Enter by second and manage（8）With hot desalinized water tank（4）Connection, vapor can（3）Enter by second Pipe（8）With hot desalinized water tank（4）Connection；The hot desalinized water tank（4）Provided with discharge nozzle（5）, condensed water discharge pipe（6）, the discharge nozzle（5）, condensed water discharge pipe （6）Respectively with heat-exchanger rig（9）Charging aperture（9-1）And water inlet（9-2）Connection.
- The heat-exchanger rig 2. albumin milk according to claim 1 liquefies, it is characterised in that：The condensed water discharge pipe（6）Bag Include the first condensed water exhaust outlet（6-1）With the second condensed water exhaust outlet（6-2）, the first condensed water exhaust outlet（6- 1）With heat-exchanger rig（9）Water inlet（9-2）Connection, the second condensed water exhaust outlet（6-2）With cyclic water tank（10）Even Connect, the first condensed water exhaust outlet（6-1）It is provided with compression pump（11）And first flowmeter（12）, the compression pump（11） And first flowmeter（12）With control device（13）Connection.
- The heat-exchanger rig 3. albumin milk according to claim 1 liquefies, it is characterised in that：The charging aperture（9-1）It is provided with Feed pump（14）And second flowmeter（15）, the feed pump（14）And second flowmeter（15）Respectively with control device（13）Even Connect.
- The heat-exchanger rig 4. albumin milk according to claim 1 liquefies, it is characterised in that：The heat-exchanger rig（9）It is provided with Heat-exchanger rig discharge nozzle（9-3）And outlet pipe（9-4）, the heat-exchanger rig discharge nozzle（9-3）And outlet pipe（9-4）It is respectively equipped with First temperature sensing device（16）With second temperature induction installation（17）, first temperature sensing device（16）And second temperature Induction installation（17）Respectively with control device（13）Connection.
- 5. according to any described albumin milk liquefaction heat-exchanger rigs of claim 1-4, it is characterised in that：The reactant adds dress Put（1）Including cold desalination water pot（1-1）, starch milk preparation tank（1-2）, it is injected into batch can（1-3）, isomerase hydration tank（1-4）, Starch milk holding vessel（1-5）, finished product evaporator（1-6）, starch milk thickens water pot（1-7）.
- The heat-exchanger rig 6. albumin milk according to claim 5 liquefies, it is characterised in that：The heat-exchanger rig（9）Positive U-shaped and The inverted U-shaped material passing tube ganged up（9-5）Be wrapped in material passing tube（9-5）On water service pipe（9-6）.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720849281.7U CN207132755U (en) | 2017-07-13 | 2017-07-13 | A kind of albumin milk liquefaction heat-exchanger rig |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720849281.7U CN207132755U (en) | 2017-07-13 | 2017-07-13 | A kind of albumin milk liquefaction heat-exchanger rig |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN207132755U true CN207132755U (en) | 2018-03-23 |
Family
ID=61634509
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201720849281.7U Expired - Fee Related CN207132755U (en) | 2017-07-13 | 2017-07-13 | A kind of albumin milk liquefaction heat-exchanger rig |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN207132755U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN114014396A (en) * | 2021-11-05 | 2022-02-08 | 中国船舶重工集团公司第七一八研究所 | Waste liquid heat pump evaporation system and temperature control method, control equipment and medium thereof |
-
2017
- 2017-07-13 CN CN201720849281.7U patent/CN207132755U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN114014396A (en) * | 2021-11-05 | 2022-02-08 | 中国船舶重工集团公司第七一八研究所 | Waste liquid heat pump evaporation system and temperature control method, control equipment and medium thereof |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| 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: 20180323 |