CN202907736U - Pressure reducing deacidification device for preparing food plant amino acid powder - Google Patents
Pressure reducing deacidification device for preparing food plant amino acid powder Download PDFInfo
- Publication number
- CN202907736U CN202907736U CN 201220630995 CN201220630995U CN202907736U CN 202907736 U CN202907736 U CN 202907736U CN 201220630995 CN201220630995 CN 201220630995 CN 201220630995 U CN201220630995 U CN 201220630995U CN 202907736 U CN202907736 U CN 202907736U
- Authority
- CN
- China
- Prior art keywords
- pipe
- tank body
- amino acid
- cold cycling
- plant amino
- 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.)
- Withdrawn - After Issue
Links
Images
Landscapes
- Coloring Foods And Improving Nutritive Qualities (AREA)
- Food Preservation Except Freezing, Refrigeration, And Drying (AREA)
Abstract
The utility model discloses a pressure reducing deacidification device for preparing food plant amino acid powder, which comprises a cylindrical tank body with a vacuum pumping hole at the top, wherein two observation windows are arranged on the outer wall of the upper part of the tank body; a large hot-cold circulating pipe and a small hot-cold circulating pipe, which are communicated up and down, are mounted on the inner wall of the lower part of the tank body; a discharge opening and a first feeding pipe are arranged at the bottom of the tank body; the first feeding pipe extends upwards from the bottom of the tank body to the middle along the outer wall; the top of the first feeding pipe is respectively in connection with a second feeding pipe and a water pipe; the other side of the water pipe is connected with a steam pipe; and valves are respectively mounted on the second feeding pipe, the water pipe and the steam pipe. The device provided by the utility model has the characteristics of convenience in operation and high production efficiency.
Description
Technical field
The utility model relates to a kind of food plant amino acid dry powder production equipment, relates in particular to food plant amino acid dry powder production equipment parts.
Background technology
Food plant amino acid dry powder refines from plant and forms, hold total disease genetic gene without anyone, thereby eliminated the possibility of genetic disease, the amino acid that is rich in is by maintenance and to repair muscle, tendon, skin, ligament etc. essential, also can improve simultaneously people's immunocompetence, reduce blood pressure, also have the effect of liver protecting toxin expelling.In the production process of plant amino acid dry powder, need to be with composite vegetative amino acid stoste simmer down to dry powder-shaped.At this moment, it is concentrated to carry out depickling by the decompression deacidification tank.
The utility model content
The technical problems to be solved in the utility model is to overcome existing defective, and a kind of easy to operate, decompression deacidifying device for the manufacture of food plant amino acid dry powder that production efficiency is high is provided.
In order to solve the problems of the technologies described above, the utility model provides following technical scheme:
Decompression deacidifying device for the manufacture of food plant amino acid dry powder, comprise tank body, the cylindrical shape of described tank body, described tank body top has vacuum pumping opening, described tank body external wall of upper portion is provided with two observation windows, described tank body lower part inwall is equipped with the large cold cycling pipe that communicates up and down, little cold cycling pipe, described tank base is provided with discharging opening and the first feed pipe, described the first feed pipe extends upwardly to the tank body middle part from tank base along its outer wall, described the first feed pipe top by pipeline respectively with the second feed pipe, water pipe connects, described water pipe opposite side is connected with steam pipe, described the second feed pipe, water pipe and steam pipe all are equipped with valve.
Further, two described observation windows are on the same side outer wall of tank body.
Further, described large cold cycling pipe is
250mm * 1, little cold cycling pipe is
50mm * 16, large cold cycling pipe periphery is evenly equipped with 16 little cold cycling pipes.
Further, the upper end of described large cold cycling pipe and little cold cycling pipe fixing welding punching steel plate, and the lower end of large cold cycling pipe and little cold cycling pipe fixing welding punching steel plate.
Further, welded seal between described punching steel plate and the inner tank wall.
Further, described the first feed pipe top is equipped with the three-way pipe that is connected with the second feed pipe, water pipe respectively.
Further, described steam pipe, water pipe, the second feed tube opening all are horizontal.
Compared with prior art, the utlity model has following beneficial effect:
Easy to operate, production efficiency is high, simple in structure, it is high that food plant amino acid reclaims quality, reaches more than 99% processing calcium sulfate and sulfate radical removing ability.
Description of drawings
Fig. 1 is that the utility model is for the manufacture of the schematic diagram of the tank body of the decompression deacidifying device of food plant amino acid dry powder;
Fig. 2 is that the utility model is for the manufacture of the schematic diagram of the decompression deacidifying device of food plant amino acid dry powder;
The specific embodiment
Below in conjunction with accompanying drawing preferred embodiment of the present utility model is described, should be appreciated that preferred embodiment described herein only is used for description and interpretation the utility model, and be not used in restriction the utility model.
As shown in Figure 1 and Figure 2, the decompression deacidifying device for the manufacture of food plant amino acid dry powder comprises tank body 14, tank body 14 cylindrical shapes, have vacuum pumping opening 1 at tank body 14 tops, tank body 14 external wall of upper portion are provided with 2, two observation windows 2 of two observation windows and are on the same side outer wall of tank body.Tank body 14 lower inner wall are equipped with large cold cycling pipe 3, little cold cycling pipe 4, and large cold cycling pipe 3, little cold cycling pipe 4 tube hubs communicate up and down, and large cold cycling pipe 3 is
250mm * 1, little cold cycling pipe 4 is
50mm * 16, large cold cycling pipe 3 peripheries are evenly equipped with 16 little cold cycling pipes 4.Fixing welding punching steel plate is adopted in the upper end of large cold cycling pipe 3 and little cold cycling pipe 4, and fixing welding punching steel plate, welded seal between punching steel plate and the inner tank wall are adopted in the lower end of large cold cycling pipe 3 and little cold cycling pipe 4.Tank body 14 bottoms are provided with discharging opening 5 and the first feed pipe 13, the first feed pipe 13 extends upwardly to the tank body middle part from tank body 14 bottoms along its outer wall, the first feed pipe 13 tops are connected with the second feed pipe 12, water pipe 11 respectively by pipeline, the first feed pipe 13 tops are equipped with the three-way pipe that is connected with the second feed pipe 12, water pipe 11 respectively, and the second steam valve 9 is installed on the first feed pipe 13.Water pipe 11 other ends are connected with steam pipe 7, and the second feed pipe 12 is equipped with takes out material valve 10, and aqueduct valve 8 is installed on the water pipe 11, and steam pipe 7 is equipped with the first steam valve 6.Steam pipe 7, water pipe 11, the second feed pipe 12 openings all are horizontal.Observation window 2, the first feed pipe 13, the second feed pipe 12, water pipe 11, steam pipe 7 all are on the same side outer wall of tank body, are convenient to the material input and output material and process.
Composite vegetative amino acid stoste enters the decompression deacidification tank by the second feed pipe 12 and the second steam valve 9, open water tube valve 8 is warming up to 50 ℃, stoste makes it produce cold and hot convection current by cold cycling pipe 3,4, boiling, if stoste is bonding with observation window 2, observation window 2 can't be observed boiling situation in the tank, at this moment, open the first steam valve 6 and clean observation window 2, in order in time observe the boiling situation.Beginning pump drainage vacuum makes in its situation that maintains 0.04Mpa in the decompression deacidification tank to keep 50 minutes, discharges by discharging opening 5, and cooling was left standstill 24 hours.Add centrifuge, water washes out composite vegetative amino acid again, and eluate is warming up to 80 ℃, sterilization, and its yield of composite vegetative amino acid finished product is 7.0%, pH value 4.7.
The above only is explanation embodiment of the present utility model; be not limited to the utility model; for a person skilled in the art; all within spirit of the present utility model and principle; any modification of doing, be equal to replacement, improvement etc., all should be included within the protection domain of the present utility model.
Claims (7)
1. for the manufacture of the decompression deacidifying device of food plant amino acid dry powder, comprise tank body, the cylindrical shape of described tank body, it is characterized in that: described tank body top has vacuum pumping opening, described tank body external wall of upper portion is provided with two observation windows, described tank body lower part inwall is equipped with the large cold cycling pipe that communicates up and down, little cold cycling pipe, described tank base is provided with discharging opening and the first feed pipe, described the first feed pipe extends upwardly to the tank body middle part from tank base along its outer wall, described the first feed pipe top by pipeline respectively with the second feed pipe, water pipe connects, described water pipe opposite side is connected with steam pipe, described the second feed pipe, water pipe and steam pipe all are equipped with valve.
2. the decompression deacidifying device for the manufacture of food plant amino acid dry powder as claimed in claim 1, it is characterized in that: two described observation windows are on the same side outer wall of tank body.
3. the decompression deacidifying device for the manufacture of food plant amino acid dry powder as claimed in claim 1, it is characterized in that: described large cold cycling pipe is
250mm * 1, little cold cycling pipe is
50mm * 16, large cold cycling pipe periphery is evenly equipped with 16 little cold cycling pipes.
4. the decompression deacidifying device for the manufacture of food plant amino acid dry powder as claimed in claim 3, it is characterized in that: the upper end of described large cold cycling pipe and little cold cycling pipe fixing welding punching steel plate, and the lower end of large cold cycling pipe and little cold cycling pipe fixing welding punching steel plate.
5. the decompression deacidifying device for the manufacture of food plant amino acid dry powder as claimed in claim 4 is characterized in that: welded seal between described punching steel plate and the inner tank wall.
6. the decompression deacidifying device for the manufacture of food plant amino acid dry powder as claimed in claim 1, it is characterized in that: described the first feed pipe top is equipped with the three-way pipe that is connected with the second feed pipe, water pipe respectively.
7. the decompression deacidifying device for the manufacture of food plant amino acid dry powder as claimed in claim 1, it is characterized in that: described steam pipe, water pipe, the second feed tube opening all are horizontal.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201220630995 CN202907736U (en) | 2012-11-26 | 2012-11-26 | Pressure reducing deacidification device for preparing food plant amino acid powder |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201220630995 CN202907736U (en) | 2012-11-26 | 2012-11-26 | Pressure reducing deacidification device for preparing food plant amino acid powder |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN202907736U true CN202907736U (en) | 2013-05-01 |
Family
ID=48156099
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 201220630995 Withdrawn - After Issue CN202907736U (en) | 2012-11-26 | 2012-11-26 | Pressure reducing deacidification device for preparing food plant amino acid powder |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN202907736U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102972619A (en) * | 2012-11-26 | 2013-03-20 | 塔城市星河生物工程有限责任公司 | Decompressing deacidification device for manufacturing food plant amino acid dry powder |
-
2012
- 2012-11-26 CN CN 201220630995 patent/CN202907736U/en not_active Withdrawn - After Issue
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102972619A (en) * | 2012-11-26 | 2013-03-20 | 塔城市星河生物工程有限责任公司 | Decompressing deacidification device for manufacturing food plant amino acid dry powder |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN106616578A (en) | Method for preparing liquid enzyme through cell wall breaking | |
| CN103333766A (en) | Brewing technique of olive brandy based on solid-state fermentation method | |
| CN202849381U (en) | Device for efficiently and comprehensively utilizing potato starch wastewater | |
| CN204550515U (en) | A kind of beer production suite of equipment | |
| CN202907736U (en) | Pressure reducing deacidification device for preparing food plant amino acid powder | |
| CN104892780A (en) | Extraction process of jujube residue crude polysaccharide | |
| CN102972619B (en) | Decompressing deacidification device for manufacturing food plant amino acid dry powder | |
| CN104073355A (en) | Extraction method of pogostemon cablin essential oil | |
| CN203893489U (en) | System for recycling waste heat in pasteurization link on basis of compression heat pump | |
| CN104193668B (en) | Macroporous resin extracts the method for L-Trp in fermented liquid | |
| CN203280774U (en) | Sterilization device for brewing jar | |
| CN207769250U (en) | A kind of stuffing rectification column with cleaning device | |
| CN204783875U (en) | Salt solution siphon circulating slot | |
| CN206173297U (en) | A energy -efficient steamed rice device for yellow rice wine | |
| CN109096353A (en) | A kind of method that continuous phase transistion extracts aurantiamarin and pectin in citrus young fruit | |
| CN104073542B (en) | It is a kind of to combine the method that microorganism solid fermentation method produces Chinese yam saponin | |
| CN201825901U (en) | Production device for heparin sodium medicine | |
| CN201971823U (en) | Pasteurizing equipment | |
| CN106723099A (en) | Inspissated juice production system | |
| CN102516354B (en) | Separation method and equipment of protein from starch sugar liquefied solution | |
| CN205516637U (en) | Tower is collected to multiple tank body phenol | |
| CN204273167U (en) | Garlic flaying machine | |
| CN204583175U (en) | A kind of production agricultural chemicals reactor | |
| CN204032256U (en) | For the thermal release pot system that oranges and tangerines Nang Bao processes | |
| CN204824813U (en) | Vegetable oil production system |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| AV01 | Patent right actively abandoned |
Granted publication date: 20130501 Effective date of abandoning: 20150121 |
|
| RGAV | Abandon patent right to avoid regrant |