CN211153611U - Whey liquid forced circulation falling film thickener - Google Patents
Whey liquid forced circulation falling film thickener Download PDFInfo
- Publication number
- CN211153611U CN211153611U CN201921909028.1U CN201921909028U CN211153611U CN 211153611 U CN211153611 U CN 211153611U CN 201921909028 U CN201921909028 U CN 201921909028U CN 211153611 U CN211153611 U CN 211153611U
- Authority
- CN
- China
- Prior art keywords
- forced circulation
- water
- pump
- whey
- falling film
- 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.)
- Active
Links
Images
Landscapes
- Dairy Products (AREA)
Abstract
The utility model provides a technical scheme that its technical problem adopted is that a whey forced circulation falling film thickener includes material jar, forced circulation pump, atomizer, pneumatic valve, No. two pneumatic valves, a temperature probe, hot-water pump, electric heating pipe, No. three pneumatic blowoff valves, condensation water pitcher, vacuum pump, vacuum controller, tubular condenser, No. two temperature probe, a pressure probe, catch water, P L C control electric cabinet, the utility model aims at a whey forced circulation falling film thickener, this kind of whey forced circulation falling film thickener can become vapor with the water in the whey under the low temperature condition and separate and then realize concentrated purpose.
Description
Technical Field
The utility model relates to an application of whey liquid falling film concentration in the whey liquid concentration processing process, in particular to a whey liquid forced circulation falling film concentrator.
Background
In the whey powder processing process, the conventional concentration method is used for processing whey liquid through triple-effect concentration, but the triple-effect concentration needs to consume a large amount of steam, the whole operation process is relatively complex, and whether the specific gravity of the feed liquid at a discharge port is influenced by the steam pressure and the feeding speed needs to be continuously detected. But a whey liquid forced circulation falling film thickener can increase the evaporation area, improves the evaporation efficiency, can fully stir mixed materials without consuming steam, discharges materials once when the specific gravity of feed liquid reaches a set value after circulating, and has simple structure and small floor area.
Disclosure of Invention
The utility model aims at a whey forced circulation falling film concentrator, this kind of whey forced circulation falling film concentrator can become vapor with the water in the whey under the low temperature condition and separate and then realize concentrated purpose.
The technical scheme adopted by the utility model for solving the technical problems is that the whey liquid forced circulation falling film thickener comprises a material tank, a forced circulation pump, an atomizer, a pneumatic valve, a temperature probe, a hot water pump, an electric heating pipe, a pneumatic blow-down valve, a condensation water tank, a vacuum pump, a vacuum controller, a tubular condenser, a temperature probe, a pressure probe, a steam-water separator and a P L C control electric cabinet.
In the scheme, the outlet of the material tank is connected with a pneumatic valve I, the pneumatic valve I is connected with a forced circulation pump, and the forced circulation pump is connected with an atomizer to form a material circulation system; under the condition that the first pneumatic valve is opened, the materials in the material tank enter the atomizer under the action of the forced circulation pump to form falling films and return to the material tank, so that the materials can finish the circulating falling films.
In the scheme, a hot water pump is connected with an outlet of an interlayer of a material tank, an electric heating pipe is connected with an outlet of the hot water pump, an interlayer water heating system is formed by connecting an outlet of the electric heating pipe with an interlayer inlet of the material tank, water in the interlayer of the material tank flows under the action of the hot water pump and then is heated under the action of the electric heating pipe, a second temperature probe continuously detects the water temperature of the interlayer and feeds the water temperature back to a P L C control electric cabinet, and the on-off of the electric heating pipe is controlled by comparing the temperature with a temperature set value in the P L C control electric cabinet.
In the scheme, the vacuum pump is connected with a vacuum controller, the vacuum controller is connected with a condensate water tank, the condensate water tank is connected with a steam-water separator through a pipeline, a first pressure probe is arranged between the condensate water tank and the steam-water separator, the steam-water separator is connected with a material tank through a pipeline to form a vacuum pumping system, and the vacuum controller and the first pressure probe compare the vacuum degree in the pipeline with a set value in a P L C control cabinet to control the starting and stopping of the vacuum pump.
The utility model discloses following beneficial effect has:
1. a forced circulation falling film thickener for whey liquid does not need to consume a large amount of steam, has low water evaporation and vaporization temperature under vacuum condition, has less denaturation of whey protein and saves energy sources at the same time.
2. A whey liquid forced circulation falling film thickener has a simple structure, is convenient to disassemble, and is easy to clean, maintain and maintain.
3. A whey liquid forced circulation falling film thickener can increase the evaporation area and improve the evaporation efficiency.
4. A whey liquid forced circulation falling film thickener can fully stir mixed materials and improve the concentration efficiency.
Drawings
FIG. 1 is a schematic structural diagram of the present invention, in which a material tank 1, a forced circulation pump 2, an atomizer 3, a pneumatic valve 4, a pneumatic valve 5 II, a temperature probe 6I, a hot water pump 7, an electric heating pipe 8, a pneumatic blow-off valve 9 III, a condensed water tank 10, a vacuum pump 11, a vacuum controller 12, a tubular condenser 13, a temperature probe 14 II, a pressure probe 15I, a steam-water separator 16, and an electric cabinet controlled by 17P L C.
Detailed Description
The present invention is further described with reference to fig. 1:
the whey liquid forced circulation falling film thickener shown in figure 1 comprises a material tank, a forced circulation pump, an atomizer, a first pneumatic valve, a second pneumatic valve, a first temperature probe, a hot water pump, an electric heating pipe, a third pneumatic blowdown valve, a condensed water tank, a vacuum pump, a vacuum controller, a tubular condenser, a second temperature probe, a first pressure probe, a steam-water separator and a P L C control electric cabinet.
The utility model discloses the working process:
after a second pneumatic valve is opened, whey enters a material tank through a feeding port to complete feeding operation, after the whey enters the material tank, the operation is carried out, namely, after a vacuum degree is set on a P L C control electric cabinet, a vacuum pumping system is clicked to start, real-time detection information of a vacuum controller and a first pressure probe is fed back to a P L C control electric cabinet, the P L C control electric cabinet controls the starting and stopping of a vacuum pump, the vacuum pump stops working when the vacuum degree reaches-0.07 mPa, the vacuum pump starts working when the vacuum degree does not reach-0.07 mPa, after the temperature is set on the P L C control electric cabinet, click heating is started, after a hot water circulating pump is started, an electric heating pipe starts heating, a second temperature probe detects an interlayer in real time, the electric heating pipe starts heating when the interlayer water temperature is lower than 75 ℃, the electric heating pipe stops heating when the interlayer water temperature is higher than 75 ℃, the material circulation is clicked on the electric cabinet to start, the first pneumatic valve starts, the first pneumatic valve is forcibly opened, the whey enters an atomizer in the material tank under the action of the atomizer, the steam-water separator, a steam-water evaporator, a small amount of the material enters a steam-vapor-water separator, and a condensate water separator, the material enters a condensate water tank under the action of a steam-vapor-water separator, and a condensate water separator, the material falling film-liquid separator, and a thin film-liquid separator is formed.
Claims (4)
1. A whey liquid forced circulation falling film thickener is characterized by comprising a material tank, a forced circulation pump, an atomizer, a first pneumatic valve, a second temperature probe, a hot water pump, an electric heating pipe, a third pneumatic blow-down valve, a condensed water tank, a vacuum pump, a vacuum controller, a tubular condenser, a second temperature probe, a first pressure probe, a steam-water separator and a P L C control electric cabinet.
2. A forced circulation falling film thickener for whey liquid according to claim 1, wherein: the outlet of the material tank is connected with a pneumatic valve I, the pneumatic valve I is connected with a forced circulation pump, and the forced circulation pump is connected with an atomizer to form a material circulation system; under the condition that the first pneumatic valve is opened, the materials in the material tank enter the atomizer under the action of the forced circulation pump to form falling films and return to the material tank, so that the materials can finish the circulating falling films.
3. The forced circulation falling film thickener for whey according to claim 1, wherein an outlet of an interlayer of a material tank is connected with a hot water pump, an outlet of the hot water pump is connected with an electric heating pipe, an outlet of the electric heating pipe is connected with an inlet of the interlayer of the material tank, a second temperature probe is arranged between the electric heating pipe and the inlet of the interlayer of the material tank to form an interlayer water heating system, water in the interlayer of the material tank flows under the action of the hot water pump and then is heated under the action of the electric heating pipe, the second temperature probe continuously detects the water temperature of the interlayer and feeds the water temperature back to a P L C control electric cabinet, and the on-off of the electric heating pipe is controlled by comparing the temperature set value in the P L C control.
4. A forced circulation falling film thickener for whey according to claim 1, wherein the vacuum pump is connected with a vacuum controller, the vacuum controller is connected with a condensate water tank, the condensate water tank is connected with a steam-water separator through a pipeline, a first pressure probe is arranged between the condensate water tank and the steam-water separator, the steam-water separator is connected with a material tank through a pipeline to form a vacuum pumping system, and the vacuum controller and the first pressure probe control the starting and stopping of the vacuum pump according to the comparison between the vacuum degree in the pipeline and a set value in a P L C control cabinet.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201921909028.1U CN211153611U (en) | 2019-10-31 | 2019-10-31 | Whey liquid forced circulation falling film thickener |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201921909028.1U CN211153611U (en) | 2019-10-31 | 2019-10-31 | Whey liquid forced circulation falling film thickener |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN211153611U true CN211153611U (en) | 2020-08-04 |
Family
ID=71815750
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201921909028.1U Active CN211153611U (en) | 2019-10-31 | 2019-10-31 | Whey liquid forced circulation falling film thickener |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN211153611U (en) |
-
2019
- 2019-10-31 CN CN201921909028.1U patent/CN211153611U/en active Active
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN111252835A (en) | Waste liquid evaporation treatment method and heating and refrigerating method in waste liquid evaporation process | |
| CN102008829A (en) | Multi-effect vacuum forced circulation evaporation device and material concentrating method thereof | |
| CN108159719A (en) | Energy-conserving efficient MVR evaporative concentration system | |
| CN207279602U (en) | A kind of closed type condensate water recovery device | |
| CN201823328U (en) | Vacuum multi-effect forced circulation evaporation device | |
| CN201301235Y (en) | Triple-effect continuous evaporative condenser | |
| CN204522328U (en) | Three grades with function of mechanical steam recompression continuous falling liquid film circulating and evaporating concentration systems | |
| CN104922921B (en) | A kind of self-loopa MVR thermo-compression evaporation systems | |
| CN211153611U (en) | Whey liquid forced circulation falling film thickener | |
| CN201519474U (en) | External circulating evaporator | |
| CN201216884Y (en) | Energy-conservation forced-air circulation liquid extract concentrating device | |
| CN111233060B (en) | Evaporator, vacuum degree, liquid level of evaporation kettle and water level detection control method of water tank | |
| CN213416350U (en) | Sewage treatment device | |
| CN203750196U (en) | Double-effect concentration device | |
| CN104329830B (en) | A kind of turbine exhaust steam waste heat recycling device and process thereof | |
| CN208396754U (en) | Steam turbine start stop system and its work system | |
| CN101289384B (en) | Use method of multiple-effect falling film concentrating device in production of lactic acid | |
| CN204910802U (en) | Self -circulation MVR heat pump evaporation system | |
| CN214512755U (en) | Heat pump double-effect evaporation concentration system with low-level heat discarding balance | |
| CN205307832U (en) | Multiple -effect forced circulation evaporator comdenstion water flash distillation heat recovery system | |
| CN203609885U (en) | Efficient forced circulation evaporator | |
| CN213492042U (en) | Three-effect concentration and evaporation device | |
| CN209428171U (en) | A kind of equipment being concentrated by evaporation electroplating wastewater using solar water heater | |
| CN206853145U (en) | Continous way medicinal extract enrichment machine | |
| CN223127257U (en) | Efficient energy-saving liquid medicine extracting and concentrating device |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20240718 Address after: Room A817, Building A, Building 4, Emerging Industry Incubator, No. 46 Huoju New Street, High tech Zone, Daqing City, Heilongjiang Province, 163000 Patentee after: Anmuji (Heilongjiang) Food Co.,Ltd. Country or region after: China Address before: 163000 room 4 819, national emerging industry incubator (Park), No. 36, torch new street, high tech Zone, Daqing City, Heilongjiang Province Patentee before: HEILONGJIANG HEYI DAIRY TECHNOLOGY CO.,LTD. Country or region before: China |
|
| TR01 | Transfer of patent right |