CN108142868A - A kind of concentrator for the processing of scallop powder - Google Patents
A kind of concentrator for the processing of scallop powder Download PDFInfo
- Publication number
- CN108142868A CN108142868A CN201711436361.0A CN201711436361A CN108142868A CN 108142868 A CN108142868 A CN 108142868A CN 201711436361 A CN201711436361 A CN 201711436361A CN 108142868 A CN108142868 A CN 108142868A
- Authority
- CN
- China
- Prior art keywords
- tank body
- concentrator
- babinet
- air
- heating tube
- 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.)
- Pending
Links
- 241000237509 Patinopecten sp. Species 0.000 title claims abstract description 24
- 235000020637 scallop Nutrition 0.000 title claims abstract description 24
- 239000000843 powder Substances 0.000 title claims abstract description 18
- 238000010438 heat treatment Methods 0.000 claims abstract description 36
- 238000000605 extraction Methods 0.000 claims abstract description 11
- 241000628997 Flos Species 0.000 claims description 16
- 238000007599 discharging Methods 0.000 claims description 10
- 238000009833 condensation Methods 0.000 claims description 6
- 230000005494 condensation Effects 0.000 claims description 6
- 239000012528 membrane Substances 0.000 claims description 6
- 238000005265 energy consumption Methods 0.000 abstract description 5
- 230000000694 effects Effects 0.000 abstract description 4
- 238000009835 boiling Methods 0.000 abstract description 3
- 238000000034 method Methods 0.000 description 7
- 238000010586 diagram Methods 0.000 description 4
- GVJHHUAWPYXKBD-UHFFFAOYSA-N (±)-α-Tocopherol Chemical compound OC1=C(C)C(C)=C2OC(CCCC(C)CCCC(C)CCCC(C)C)(C)CCC2=C1C GVJHHUAWPYXKBD-UHFFFAOYSA-N 0.000 description 2
- 206010012735 Diarrhoea Diseases 0.000 description 2
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 2
- AUNGANRZJHBGPY-SCRDCRAPSA-N Riboflavin Chemical compound OC[C@@H](O)[C@@H](O)[C@@H](O)CN1C=2C=C(C)C(C)=CC=2N=C2C1=NC(=O)NC2=O AUNGANRZJHBGPY-SCRDCRAPSA-N 0.000 description 2
- 150000001720 carbohydrates Chemical class 0.000 description 2
- HVYWMOMLDIMFJA-DPAQBDIFSA-N cholesterol Chemical compound C1C=C2C[C@@H](O)CC[C@]2(C)[C@@H]2[C@@H]1[C@@H]1CC[C@H]([C@H](C)CCCC(C)C)[C@@]1(C)CC2 HVYWMOMLDIMFJA-DPAQBDIFSA-N 0.000 description 2
- 201000010099 disease Diseases 0.000 description 2
- 208000037265 diseases, disorders, signs and symptoms Diseases 0.000 description 2
- 230000017525 heat dissipation Effects 0.000 description 2
- 230000000050 nutritive effect Effects 0.000 description 2
- 238000003756 stirring Methods 0.000 description 2
- 210000002784 stomach Anatomy 0.000 description 2
- 206010000060 Abdominal distension Diseases 0.000 description 1
- OYPRJOBELJOOCE-UHFFFAOYSA-N Calcium Chemical compound [Ca] OYPRJOBELJOOCE-UHFFFAOYSA-N 0.000 description 1
- AUNGANRZJHBGPY-UHFFFAOYSA-N D-Lyxoflavin Natural products OCC(O)C(O)C(O)CN1C=2C=C(C)C(C)=CC=2N=C2C1=NC(=O)NC2=O AUNGANRZJHBGPY-UHFFFAOYSA-N 0.000 description 1
- 201000004624 Dermatitis Diseases 0.000 description 1
- 206010013786 Dry skin Diseases 0.000 description 1
- FYYHWMGAXLPEAU-UHFFFAOYSA-N Magnesium Chemical compound [Mg] FYYHWMGAXLPEAU-UHFFFAOYSA-N 0.000 description 1
- PVNIIMVLHYAWGP-UHFFFAOYSA-N Niacin Chemical compound OC(=O)C1=CC=CN=C1 PVNIIMVLHYAWGP-UHFFFAOYSA-N 0.000 description 1
- 208000003251 Pruritus Diseases 0.000 description 1
- 229930003427 Vitamin E Natural products 0.000 description 1
- HCHKCACWOHOZIP-UHFFFAOYSA-N Zinc Chemical compound [Zn] HCHKCACWOHOZIP-UHFFFAOYSA-N 0.000 description 1
- 208000019790 abdominal distention Diseases 0.000 description 1
- 230000004596 appetite loss Effects 0.000 description 1
- 229910052791 calcium Inorganic materials 0.000 description 1
- 239000011575 calcium Substances 0.000 description 1
- 230000002490 cerebral effect Effects 0.000 description 1
- 238000007600 charging Methods 0.000 description 1
- 235000012000 cholesterol Nutrition 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 238000000151 deposition Methods 0.000 description 1
- 230000037336 dry skin Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000001704 evaporation Methods 0.000 description 1
- 230000008020 evaporation Effects 0.000 description 1
- 206010016256 fatigue Diseases 0.000 description 1
- 235000013305 food Nutrition 0.000 description 1
- WIGCFUFOHFEKBI-UHFFFAOYSA-N gamma-tocopherol Natural products CC(C)CCCC(C)CCCC(C)CCCC1CCC2C(C)C(O)C(C)C(C)C2O1 WIGCFUFOHFEKBI-UHFFFAOYSA-N 0.000 description 1
- 229910052742 iron Inorganic materials 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 235000021266 loss of appetite Nutrition 0.000 description 1
- 208000019017 loss of appetite Diseases 0.000 description 1
- 229910052749 magnesium Inorganic materials 0.000 description 1
- 239000011777 magnesium Substances 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 229960003512 nicotinic acid Drugs 0.000 description 1
- 235000001968 nicotinic acid Nutrition 0.000 description 1
- 239000011664 nicotinic acid Substances 0.000 description 1
- 230000019612 pigmentation Effects 0.000 description 1
- 238000009700 powder processing Methods 0.000 description 1
- 102000004169 proteins and genes Human genes 0.000 description 1
- 108090000623 proteins and genes Proteins 0.000 description 1
- 238000005086 pumping Methods 0.000 description 1
- 239000003507 refrigerant Substances 0.000 description 1
- 229960002477 riboflavin Drugs 0.000 description 1
- 235000019192 riboflavin Nutrition 0.000 description 1
- 239000002151 riboflavin Substances 0.000 description 1
- 230000000630 rising effect Effects 0.000 description 1
- 230000009759 skin aging Effects 0.000 description 1
- 206010040872 skin infection Diseases 0.000 description 1
- 206010040882 skin lesion Diseases 0.000 description 1
- 231100000444 skin lesion Toxicity 0.000 description 1
- 238000006467 substitution reaction Methods 0.000 description 1
- 229940088594 vitamin Drugs 0.000 description 1
- 229930003231 vitamin Natural products 0.000 description 1
- 235000013343 vitamin Nutrition 0.000 description 1
- 239000011782 vitamin Substances 0.000 description 1
- 229940046009 vitamin E Drugs 0.000 description 1
- 235000019165 vitamin E Nutrition 0.000 description 1
- 239000011709 vitamin E Substances 0.000 description 1
- 150000003722 vitamin derivatives Chemical class 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
- 238000004804 winding Methods 0.000 description 1
- 239000011701 zinc Substances 0.000 description 1
- 229910052725 zinc Inorganic materials 0.000 description 1
Classifications
-
- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23L—FOODS, FOODSTUFFS, OR NON-ALCOHOLIC BEVERAGES, NOT COVERED BY SUBCLASSES A21D OR A23B-A23J; THEIR PREPARATION OR TREATMENT, e.g. COOKING, MODIFICATION OF NUTRITIVE QUALITIES, PHYSICAL TREATMENT; PRESERVATION OF FOODS OR FOODSTUFFS, IN GENERAL
- A23L17/00—Food-from-the-sea products; Fish products; Fish meal; Fish-egg substitutes; Preparation or treatment thereof
- A23L17/40—Shell-fish
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D1/00—Evaporating
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D1/00—Evaporating
- B01D1/30—Accessories for evaporators ; Constructional details thereof
Landscapes
- Chemical & Material Sciences (AREA)
- Life Sciences & Earth Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Marine Sciences & Fisheries (AREA)
- Zoology (AREA)
- Health & Medical Sciences (AREA)
- Nutrition Science (AREA)
- Engineering & Computer Science (AREA)
- Food Science & Technology (AREA)
- Polymers & Plastics (AREA)
- Processing Of Meat And Fish (AREA)
Abstract
The present invention relates to technical field of aquatic product processing, and in particular to a kind of concentrator for the processing of scallop powder, including tank body, thermocirculator, extraction element and for the concentration tank to be made to keep the air extractor of low pressure or vacuum state；The thermocirculator includes air inlet pipe, air outlet pipe, connector, driving motor, drive shaft and at least one heating tube, and heating tube is U-tube；The connector is made of babinet and the cover to match with babinet；The both ends of the heating tube are fixed in the cover, and the cover rotates under the drive of drive shaft on the babinet.Advantageous effect：It is fast to save energy consumption, heating speed.During hot gas Rapid Circulation, heat exchange constantly is carried out with the original solution in tank body, is allowed to heat up in proper order.Made to make the boiling point of original solution reduce in vacuum or low-pressure state in tank body with air extractor, solution, which is easily evaporated and does not need to very high temperature, can just evaporate, while ensure that nutriment is not destroyed.
Description
Technical field
The present invention relates to technical field of aquatic product processing, and in particular to a kind of concentrator for the processing of scallop powder.
Background technology
Scallop is a kind of common aquatic food, and nutritive value is very high.Every 2.60 grams of 100 grams of scallop carbohydrate containings,
0.60 gram of fat, 11.10 grams of protein, 1.85 milligrams of vitamin e1,0.10 milligram of riboflavin, 0.20 milligram of niacin, cholesterol
140.00 milligrams, 39.00 milligrams of magnesium, 142.00 milligrams of calcium, 7.20 milligrams of iron, 11.69 milligrams of zinc.
The carbohydrate that scallop is rich in can maintain the necessary energy of cerebral function, apply also for deficiency-weakness of spleen-QI, transporting
The diseases such as the abdominal fullness and distention caused by powerless, diarrhea with loose stool, loss of appetite, lassitude of the limbs and weakness.Warm stomach treats stomach cold disease.It contains abundant
Vitamin E, inhibit skin aging, prevent pigmentation.Drive away because of caused by skin allergy or infection dry skin and
The skin lesions such as itch.
The high nutritive value of scallop is pursued by market, is now fabricated to battalion by the way that scallop is processed into powder in the market
The product of supporting.
However the process of scallop powder is complicated, process equipment is expensive, and the price for making scallop powder product is also more expensive.It is existing
The concentrator of scallop powder processing is useful for, complicated, high energy consumption causes equipment and high processing costs, and processing efficiency
Lowly.Disadvantages mentioned above is an important factor for current influence scallop powder yield is low.
Invention content
The purpose of the present invention is to solve current scallop concentrator, complicated, high energy consumption causes equipment and processing
The problem of of high cost, provides a kind of concentrator for the processing of scallop powder.
In order to reach foregoing invention purpose, the present invention uses following technical scheme：
A kind of concentrator for the processing of scallop powder, including tank body, thermocirculator, extraction element and for making
State the air extractor that tank body keeps low pressure or vacuum state；Floss hole is equipped at the top of the tank body, floss hole is filled with the extraction
It puts connected；The thermocirculator includes air inlet pipe, air outlet pipe, connector, driving motor, drive shaft and at least one heating
Pipe, heating tube is U-tube；The connector is set in the tank body, the air inlet pipe and air outlet pipe with the connector
Connection, the head end of the air inlet pipe connect with the tail end of the air outlet pipe；The air inlet pipe is equipped with heater, the air outlet pipe
It is equipped with air blower；The connector is made of babinet and the cover to match with babinet, and the inner loop of the babinet is arranged with one
A interior connecting cavity and an outer connecting cavity, the air inlet pipe and air outlet pipe connect respectively with the interior connecting cavity and the outer connecting cavity
It is logical；The both ends of the heating tube are fixed in the cover, and two nozzles of the heating tube respectively with the interior connecting cavity
It is connected with the outer connecting cavity；The drive shaft runs through the babinet, and one end of drive shaft connect with the cover, the other end and
The driving motor connection, the cover rotate under the drive of drive shaft on the babinet.
Preferably, the extraction element includes the discharging pipeline and outlet pipeline that are connected with the floss hole, outlet pipeline
It is set to the top of the discharging pipeline.
Preferably, the filter membrane for closing the entrance of the outlet pipeline is equipped at the nozzle of the outlet pipeline.
Preferably, condensation endless tube is cased on the outer tube wall of the discharging pipeline and outlet pipeline.
Preferably, anti-return plate is equipped at the floss hole.
Preferably, the side wall of the tank body is equipped with feed inlet, and feed inlet is equipped with inlet valve.
Preferably, drain valve is equipped at the floss hole.
Compared with prior art, the present invention advantageous effect is：By thermocirculator, energy consumption can be saved, and heat speed
Degree is fast, during hot gas Rapid Circulation, constantly carries out heat exchange with the original solution in tank body, is allowed to heat up in proper order.With pumping
Device of air makes to make the boiling point of original solution reduce, solution is easily evaporated and does not need to very in vacuum or low-pressure state in tank body
High temperature can just evaporate, while ensure that nutriment is not destroyed.Heat dissipation area is increased by the heating tube of more u shapes,
Original solution can be evenly heated, and the efficiency of heating surface is high.By heating tube setting on the connectors, make heating tube molten with the original in tank body
While liquid carries out heat exchange, original solution can also be stirred, prevent original solution from depositing, and without once adding additional heat dissipation
Branch pipe is with regard to that can complete the circulation of hot-air.
Description of the drawings
Fig. 1 is the structure diagram of the present invention；
Fig. 2 is the connector construction schematic diagram of the present invention；
Fig. 3 is the vertical view of the cover of the present invention；
Fig. 4 is the vertical view of the babinet of the present invention；
Fig. 5 is the outlet pipeline structure schematic diagram of the present invention；
Fig. 6 is the schematic diagram of multiple heating pipe mounting structures of the present invention；
Fig. 7 is the vertical view of multiple heating pipe mounting structures of the present invention.
In figure：1 tank body, 2 drain valves, 3 extraction elements, 4 air extractors, 5 floss holes, 6 air inlet pipe, 7 air outlet pipes, 8 connections
Device, 9 driving motors, 10 drive shafts, 11 heating tubes, 12 heaters, 13 air blowers, 14 babinets, 15 covers, connecting cavity in 16,17
Outer connecting cavity, 18 discharging pipelines, 19 outlet pipelines, 20 filter membranes, 21 condensation endless tubes, 22 anti-return plates, 23 feed inlets, 24 chargings
Valve.
Specific embodiment
Explanation is further described to technical scheme of the present invention below by specific embodiment.
The present embodiment is as shown in Figures 1 to 5：A kind of concentrator for the processing of scallop powder has row including top
The tank body 1 of mouth 5 is put, the side wall of tank body 1 is equipped with feed inlet 23, and feed inlet 23 is equipped with inlet valve 24, for controlling original solution
Conveying.The tank body 1 is transparent jar, can be from the concentration process inside external observation.
Equipment further includes the air extractor 4 for the tank body 1 to be made to keep vacuum state.Made in tank body 1 with air extractor 4
Under vacuum state, make the boiling point of original solution reduce, solution, which is easily evaporated and does not need to very high temperature, can just evaporate, together
When ensure nutriment be not destroyed.Steam after the controllable evaporation of drain valve 2 at the floss hole 5 at 1 top of tank body into
Row discharge.Floss hole 5 is connected with the extraction element 3.
Equipment further includes the thermocirculator, and thermocirculator includes air inlet pipe 6, heating tube 11, air outlet pipe 7, connection
Device 8, driving motor 9, drive shaft 10 and a heating tube 11, heating tube 11 are U-tube.
The connector 8 is set to the bottom in the tank body 1, the air inlet pipe 6 and air outlet pipe 7 with the connector
8 connections, the head end of the air inlet pipe 6 connect with the tail end of the air outlet pipe 7；The air inlet pipe 6 is equipped with heater 12, described
Air outlet pipe 7 is equipped with air blower 13.
The connector 8 is made of babinet 14 and the cover to match with babinet 14 15, and cover 15 is sealed with the babinet 14
Cooperation, there are one interior connecting cavity 16 and an outer connecting cavity 17, the air inlet pipe 6 and outlets for the inner loop winding of the babinet 14
Pipe 7 connects respectively with the interior connecting cavity 16 and the outer connecting cavity 17；The heating tube 11 is plugged on described by its both ends
In cover 15, and two nozzles of the heating tube 11 pass through cover 15 respectively with the interior connecting cavity 16 and the outer connecting cavity
17 connections.
Hot-air constantly enters from air inlet pipe 6 in the interior connecting cavity 16 in connector 8, then from heating tube 11 wherein
One nozzle enters heating tube 11, carries out heat exchange in the heating tube 11 with the original solution in the tank body 1, then from heating tube 11
Another nozzle enter in the outer connecting cavity 17 of connector 8, deliver into air outlet pipe 7.
At this point, the drive shaft 10 runs through the babinet 14, one end of drive shaft 10 is connect with the cover 15, the other end
It is connect with the driving motor 9, the cover 15 rotates under the drive of drive shaft 10 on the babinet 14.Heating tube 11 with
Rotated with cover 15, in rotation process, two nozzles of the heating tube 11 always with the interior connecting cavity 16 and the outer company
Chamber 17 is connect to connect.Heating tube 11 can stir original solution in rotation process, so as not to deposit, and accelerate heat exchange, make
Original solution uniformly heats up, and the efficiency of heating surface is high.
Heater 12 is passed through air inlet pipe 6 after air is heated, the hot-air in air inlet pipe 6 enters in heating tube 11, in tank
It radiates in body 1, original solution is heated.Under the action of air blower 13, air circulation circulation, hot-gas recycle process
In, still there is certain temperature from the interior air out of tank body 1, be passed in heater 12, the energy consumption of heater 12 can be reduced,
Accelerate atmosphere temperature rising simultaneously.
Equipment further includes the extraction element 3, extraction element 3, including the discharging pipeline 18 that is connected with the floss hole 5 and
Outlet pipeline 19, outlet pipeline 19 are set to the top of the discharging pipeline 18.Being equipped at the nozzle of the outlet pipeline 19 will
The filter membrane 20 of 19 entrance of the outlet pipeline closing, filter membrane 20 allow hydrone to pass through.The outer tube of the outlet pipeline 19
Condensation endless tube 21 is cased on wall, 21 outer wall of condensation endless tube is equipped with the transfer pipeline for conveying refrigerant.At the floss hole 5 also
Equipped with anti-return plate 22.Anti-return plate 22 can prevent opposing steam flow.
Steam is discharged by floss hole 5, is filtered by filter membrane 20, and water vapour enters in outlet pipeline 19, steam respectively into
Enter in outlet pipeline 19 and discharging pipeline 18.Steam is cooled down by condensation endless tube 21, is concentrated from discharging pipeline 18
Solution afterwards.
As shown in Figure 6, Figure 7, on the basis of above-described embodiment, can be added by increasing the quantity of heating tube 11 to improve
Thermal effect and mixing effect can set the heating tube 11 of 6 U-shapeds, increase heat exchange area, and can more effectively stir original
Solution.
The above, the only present invention preferably specific embodiment mode, but protection scope of the present invention is not limited to
This, any one skilled in the art in the technical scope disclosed by the present invention, according to the technique and scheme of the present invention
And its improve design and be subject to equivalent substitution or change, should all it cover within the scope of the present invention.
Claims (7)
1. a kind of concentrator for the processing of scallop powder, which is characterized in that including tank body (1), thermocirculator, extraction dress
Put (3) and for the tank body (1) to be made to keep the air extractor (4) of low pressure or vacuum state；
Floss hole (5) is equipped at the top of the tank body (1), floss hole (5) is connected with the extraction element (3)；
The thermocirculator include air inlet pipe (6), air outlet pipe (7), connector (8), driving motor (9), drive shaft (10) and
At least one heating tube (11), heating tube (11) are U-tube；
The connector (8) is set in the tank body (1), the air inlet pipe (6) and air outlet pipe (7) with the connector
(8) it connects, the head end of the air inlet pipe (6) connects with the tail end of the air outlet pipe (7)；The air inlet pipe (6) is equipped with heating
Device (12), the air outlet pipe (7) are equipped with air blower (13)；
The connector (8) is made of babinet (14) and the cover (15) to match with babinet (14), the inside of the babinet (14)
Around setting there are one interior connecting cavity (16) and an outer connecting cavity (17), the air inlet pipe (6) and air outlet pipe (7) respectively with it is described
Interior connecting cavity (16) connects with the outer connecting cavity (17)；The both ends of the heating tube (11) are fixed in the cover (15),
And two nozzles of the heating tube (11) are connected respectively with the interior connecting cavity (16) and the outer connecting cavity (17)；
The drive shaft (10) connect through the babinet (14), one end of drive shaft (10) with the cover (15), the other end
It is connect with the driving motor (9), the cover (15) rotates under the drive of drive shaft (10) on the babinet (14).
A kind of 2. concentrator for the processing of scallop powder according to claim 1, which is characterized in that the extraction dress
It puts (3) and includes the discharging pipeline (18) connected with the floss hole (5) and outlet pipeline (19), outlet pipeline (19) is set to institute
State the top of discharging pipeline (18).
A kind of 3. concentrator for the processing of scallop powder according to claim 2, which is characterized in that the outlet pipe
The filter membrane (20) for closing the entrance of the outlet pipeline (19) is equipped at the nozzle on road (19).
A kind of 4. concentrator for the processing of scallop powder according to claim 2, which is characterized in that the discharge nozzle
Condensation endless tube (21) is cased on the outer tube wall of road (18) and outlet pipeline (19).
5. according to a kind of concentrator processed for scallop powder of claim 1-4 any one of them, which is characterized in that institute
It states and anti-return plate (22) is equipped at floss hole (5).
6. according to a kind of concentrator processed for scallop powder of claim 1-4 any one of them, which is characterized in that institute
The side wall for stating tank body (1) is equipped with feed inlet (23), and feed inlet (23) is equipped with inlet valve (24).
7. according to a kind of concentrator processed for scallop powder of claim 1-4 any one of them, which is characterized in that institute
It states and drain valve (2) is equipped at floss hole (5).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201711436361.0A CN108142868A (en) | 2017-12-26 | 2017-12-26 | A kind of concentrator for the processing of scallop powder |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201711436361.0A CN108142868A (en) | 2017-12-26 | 2017-12-26 | A kind of concentrator for the processing of scallop powder |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN108142868A true CN108142868A (en) | 2018-06-12 |
Family
ID=62463160
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201711436361.0A Pending CN108142868A (en) | 2017-12-26 | 2017-12-26 | A kind of concentrator for the processing of scallop powder |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN108142868A (en) |
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| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| KR200191771Y1 (en) * | 2000-03-03 | 2000-08-16 | 김동환 | Medicinal Herb Concentrate Powder Maker |
| CN102989184A (en) * | 2012-12-04 | 2013-03-27 | 湖北民族学院 | Energy-saving and environment-friendly falling film type evaporation and concentration device and method |
| CN202961922U (en) * | 2012-12-04 | 2013-06-05 | 湖北民族学院 | Energy-saving and environmentally-friendly falling-film type evaporation and concentration device |
| CN204121787U (en) * | 2014-09-10 | 2015-01-28 | 宁波立华植物提取技术有限公司 | A kind of board-like high-efficiency evaporator concentrated for ginseng extract |
| CN104436715A (en) * | 2013-09-13 | 2015-03-25 | 天津博盛源化工有限公司 | Novel condensation pot |
| CN205373351U (en) * | 2016-01-20 | 2016-07-06 | 辛后安 | Thermal balance disc drying -machine |
| CN205993565U (en) * | 2016-06-20 | 2017-03-08 | 江西恒顶食品有限公司 | A kind of enzymolysis oatmeal clean energy-saving economic benefits and social benefits external circulation evaporation enrichment facility |
| CN206262116U (en) * | 2016-11-18 | 2017-06-20 | 天津嘉深保科技发展有限公司 | A kind of enrichment facility of food production |
| CN206366200U (en) * | 2016-11-29 | 2017-08-01 | 栾云鹏 | A kind of Gueldenstaedtia verna extracts active ingredients heat concentration tank |
-
2017
- 2017-12-26 CN CN201711436361.0A patent/CN108142868A/en active Pending
Patent Citations (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| KR200191771Y1 (en) * | 2000-03-03 | 2000-08-16 | 김동환 | Medicinal Herb Concentrate Powder Maker |
| CN102989184A (en) * | 2012-12-04 | 2013-03-27 | 湖北民族学院 | Energy-saving and environment-friendly falling film type evaporation and concentration device and method |
| CN202961922U (en) * | 2012-12-04 | 2013-06-05 | 湖北民族学院 | Energy-saving and environmentally-friendly falling-film type evaporation and concentration device |
| CN104436715A (en) * | 2013-09-13 | 2015-03-25 | 天津博盛源化工有限公司 | Novel condensation pot |
| CN204121787U (en) * | 2014-09-10 | 2015-01-28 | 宁波立华植物提取技术有限公司 | A kind of board-like high-efficiency evaporator concentrated for ginseng extract |
| CN205373351U (en) * | 2016-01-20 | 2016-07-06 | 辛后安 | Thermal balance disc drying -machine |
| CN205993565U (en) * | 2016-06-20 | 2017-03-08 | 江西恒顶食品有限公司 | A kind of enzymolysis oatmeal clean energy-saving economic benefits and social benefits external circulation evaporation enrichment facility |
| CN206262116U (en) * | 2016-11-18 | 2017-06-20 | 天津嘉深保科技发展有限公司 | A kind of enrichment facility of food production |
| CN206366200U (en) * | 2016-11-29 | 2017-08-01 | 栾云鹏 | A kind of Gueldenstaedtia verna extracts active ingredients heat concentration tank |
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Application publication date: 20180612 |