CN105031958A - Falling-film concentration device - Google Patents
Falling-film concentration device Download PDFInfo
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- CN105031958A CN105031958A CN201510363490.6A CN201510363490A CN105031958A CN 105031958 A CN105031958 A CN 105031958A CN 201510363490 A CN201510363490 A CN 201510363490A CN 105031958 A CN105031958 A CN 105031958A
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- baffle
- housing
- baffle plate
- shell
- feed pipe
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Abstract
The invention relates to a falling-film concentration device, in particular to a falling-film concentration device for concentrating liquid food. The falling-film concentration device comprises a shell and a separator. A first baffle plate and a second baffle plate are arranged in an inner cavity of the shell. A heating pipe is arranged in the inner cavity of the shell between the first baffle plate and the second baffle plate. A steam inlet is formed in the side wall of the shell between the first baffle plate and the second baffle plate, and a condensed water outlet is formed in the lower part of the side wall of the shell between the first baffle plate and the second baffle plate. A discharging opening is formed in the bottom of the side wall of the shell, and the discharging opening is connected with a feeding opening of the separator by virtue of a pipeline. The falling-film concentration device is characterized in that the top of the shell is provided with a feeding pipe, the lower end of the feeding pipe is arranged in the inner cavity of the shell above the first baffle plate, the lower end of the feeding pipe is connected with a nozzle, the upper end of the feeding pipe extends out through the top of the shell, and the upper end of the feeding pipe is connected to a discharging opening of a pressurizing pump. The falling-film concentration device is used for concentrating a material, so that the material can uniformly enter each heating pipe, and the working efficiency is relatively high.
Description
Technical field
The present invention relates to a kind of enrichment facility, is the falling film type enrichment facility that liquid towards food carries out concentrating specifically.
Background technology
All know at food processing field; a large amount of moisture is had in some liquid materials or semi-finished product (as Juice, milk etc.); for the ease of storage and transport, usually need to carry out concentration to these liquid materials or semi-finished product, this can use falling film type enrichment facility usually.
At present, the falling film type enrichment facility used in industry comprises housing and separator.Have in the inner chamber of described housing in the first horizontally disposed baffle plate and second baffle, the first baffle plate is positioned at the top of second baffle, and the surrounding of the first baffle plate and second baffle all with between inner walls coordinates in fixing seal.The housing cavity be arranged between the first plate washer and second baffle has and is no less than two in the vertical heating tubes arranged, the first baffle plate that heating tube upper end is corresponding all there is the first through hole, the upper end of heating tube is positioned at corresponding first through hole respectively, the second baffle that the lower end of heating tube is corresponding all has the second through hole, and the lower end of heating tube is positioned at corresponding second through hole respectively.Be positioned in the housing sidewall between the first plate washer and second baffle and have steam-gas inlet, condensation-water drain is arranged at the bottom being positioned at the housing sidewall between the first plate washer and second baffle.The sidewall bottom of described housing has discharging opening, and discharging opening is connected by the charging aperture of pipeline with described separator, and charging aperture is arranged at the top of the sidewall of housing.During use, first material to be concentrated is entered into housing from charging aperture, in steam-gas inlet, in the inner chamber of housing, pour into heating steam simultaneously, then due to the effect of gravity, material flows downward along the inwall of heating tube, material is heated to boiling by heating steam rapidly while flowing downward, thus portion of water is wherein become steam, material and steam enter into separator from discharging opening afterwards, material after finally concentrating is discharged from the discharge gate of separator, and steam is discharged from the exhaust outlet of separator.This falling film type enrichment facility does not have guiding device, so the material entering into each heating tube is usually uneven, operating efficiency is lower.
Summary of the invention
The technical problem to be solved in the present invention is to provide a kind of falling film type enrichment facility, and use this falling film type enrichment facility to concentrate material, material can be made to enter into each heating tube uniformly, and operating efficiency is higher.
For solving the problem, provide following technical scheme:
Falling film type enrichment facility of the present invention comprises housing and separator.Have in the inner chamber of described housing in the first horizontally disposed baffle plate and second baffle, the first baffle plate is positioned at the top of second baffle, and the surrounding of the first baffle plate and second baffle all with between inner walls coordinates in fixing seal.The housing cavity be arranged between the first plate washer and second baffle has and is no less than two in the vertical heating tubes arranged, the first baffle plate that heating tube upper end is corresponding all there is the first through hole, the upper end of heating tube is positioned at corresponding first through hole respectively, the second baffle that the lower end of heating tube is corresponding all has the second through hole, and the lower end of heating tube is positioned at corresponding second through hole respectively.Be positioned in the housing sidewall between the first plate washer and second baffle and have steam-gas inlet, condensation-water drain is arranged at the bottom being positioned at the housing sidewall between the first plate washer and second baffle.The sidewall bottom of described housing has discharging opening, and discharging opening is connected by the charging aperture of pipeline with described separator.Be characterized in that the top of described housing has in the vertical feed pipe arranged, the lower end of feed pipe is arranged in the housing cavity above first gear plate, and the lower end of feed pipe is connected with nozzle, the oral area of nozzle down, the upper end of feed pipe extends through the top of housing, and the upper end of feed pipe is connected with the discharging opening of a force (forcing) pump.
Take above scheme, have the following advantages:
Case top due to falling film type enrichment facility of the present invention has in the vertical feed pipe arranged, the lower end of feed pipe is arranged in the housing cavity above first gear plate, the lower end of its feed pipe is connected with nozzle, the oral area of nozzle down, the upper end of feed pipe extends through the top of housing, and the upper end of feed pipe is connected with the charging aperture of a force (forcing) pump.During use, start force (forcing) pump, be sent in force (forcing) pump by material to be concentrated and pressurize, the material after pressurization is injected to each corner of the housing cavity above the first baffle plate through nozzle, thus make material enter into each heating tube uniformly, thus improve the efficiency of work.
Accompanying drawing explanation
Fig. 1 is the structural representation of falling film type enrichment facility of the present invention.
Detailed description of the invention
Below in conjunction with accompanying drawing, the present invention is described in further detail.
As shown in Figure 1, falling film type enrichment facility of the present invention comprises housing 1 and separator 9.Be provided with in the first horizontally disposed baffle plate 3 in the inner chamber of described housing 1 and second baffle 10, first baffle plate 3 is positioned at the top of second baffle 10, the surrounding of the first baffle plate 3 and second baffle 10 all with between housing 1 inwall coordinates in fixing seal.Housing 1 inner chamber be arranged between the first plate washer and second baffle 10 has and is no less than two in the vertical heating tubes 7 arranged, the first baffle plate 3 that heating tube 7 upper end is corresponding all there is the first through hole, the upper end of heating tube 7 is positioned at corresponding first through hole respectively, the second baffle 10 that the lower end of heating tube 7 is corresponding is all processed with the second through hole, and the lower end of heating tube 7 is positioned at corresponding second through hole respectively.Be positioned on housing 1 sidewall between the first plate washer and second baffle 10 and have steam-gas inlet 2, the bottom being positioned at housing 1 sidewall between the first plate washer and second baffle 10 is processed with condensation-water drain 8.The sidewall bottom of described housing 1 has discharging opening, and discharging opening is connected by the charging aperture of pipeline with described separator 9.The top of described housing 1 has in the vertical feed pipe 5 arranged, the lower end of feed pipe 5 is arranged in housing 1 inner chamber above first gear plate 3, and the lower end of feed pipe 5 is connected with nozzle 6, the oral area of nozzle 6 down, the upper end of feed pipe 5 extends through the top of housing 1, and the upper end of feed pipe 5 is connected with the discharging opening of a force (forcing) pump 4.
During use, first, material to be concentrated is sent to feed pipe 5 from the upper end of feed pipe 5, starts force (forcing) pump 4 pairs of materials simultaneously and pressurize.Then, the material after pressurization enters into housing 1 through nozzle 6, meanwhile, in steam-gas inlet 2, pours into heating steam in the inner chamber of housing 1.Then, due to the effect of gravity, material flows downward along the inwall of heating tube 7, and material is heated to boiling by heating steam rapidly while flowing downward, thus portion of water is wherein become steam.Afterwards, material and steam enter into separator 9 from discharging opening.Finally, the material after concentrated is discharged from the discharge gate of separator 9, and steam is discharged from the exhaust outlet of separator 9.
Claims (1)
1. a falling film type enrichment facility, comprises housing (1) and separator (9); Have in horizontally disposed the first baffle plate (3) and second baffle (10) in the inner chamber of described housing (1), first baffle plate (3) is positioned at the top of second baffle (10), and the surrounding of the first baffle plate (3) and second baffle (10) all with between housing (1) inwall coordinates in fixing seal; Housing (1) inner chamber be arranged between the first plate washer and second baffle (10) has and is no less than two in the vertical heating tubes (7) arranged, the first baffle plate (3) that heating tube (7) upper end is corresponding all there is the first through hole, the upper end of heating tube (7) is positioned at corresponding first through hole respectively, the second baffle (10) that the lower end of heating tube (7) is corresponding all has the second through hole, and the lower end of heating tube (7) is positioned at corresponding second through hole respectively; Be positioned on housing (1) sidewall between the first plate washer and second baffle (10) and have steam-gas inlet (2), condensation-water drain (8) is arranged at the bottom being positioned at housing (1) sidewall between the first plate washer and second baffle (10); The sidewall bottom of described housing (1) has discharging opening, and discharging opening is connected by the charging aperture of pipeline with described separator (9); It is characterized in that the top of described housing (1) has in the vertical feed pipe (5) arranged, the lower end of feed pipe (5) is arranged in housing (1) inner chamber of first gear plate (3) top, and the lower end of feed pipe (5) is connected with nozzle (6), the oral area of nozzle (6) down, the upper end of feed pipe (5) extends through the top of housing (1), and the upper end of feed pipe (5) is connected with the discharging opening of a force (forcing) pump (4).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201510363490.6A CN105031958A (en) | 2015-06-29 | 2015-06-29 | Falling-film concentration device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201510363490.6A CN105031958A (en) | 2015-06-29 | 2015-06-29 | Falling-film concentration device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN105031958A true CN105031958A (en) | 2015-11-11 |
Family
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201510363490.6A Pending CN105031958A (en) | 2015-06-29 | 2015-06-29 | Falling-film concentration device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN105031958A (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110038315A (en) * | 2019-04-02 | 2019-07-23 | 天津科技大学 | The tube type falling-film vaporising device of a variety of media can be handled simultaneously |
| CN110063405A (en) * | 2019-05-16 | 2019-07-30 | 江苏美德实医疗科技有限公司 | A kind of device and method of industrial efficient batch continuous production collagen |
Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3332469A (en) * | 1966-09-13 | 1967-07-25 | Rosenblad Corp | Falling film type heat exchanger |
| GB1163364A (en) * | 1967-11-03 | 1969-09-04 | Axel Everhard Rosenblad | Falling Film Evaporator |
| CN2780284Y (en) * | 2005-03-30 | 2006-05-17 | 宜兴市格兰特干燥浓缩设备有限公司 | Improved falling film evaporator |
| WO2014013502A2 (en) * | 2012-07-18 | 2014-01-23 | M/S Raj Process Equipments & Systems Pvt. Ltd. | Non-clog extra long tube falling film evaporation system |
| CN203677967U (en) * | 2014-02-26 | 2014-07-02 | 成都华高生物制品有限公司 | Single-effect falling film concentrator |
| CN204767494U (en) * | 2015-06-29 | 2015-11-18 | 江苏楷益智能科技有限公司 | Falling liquid film formula enrichment facility |
-
2015
- 2015-06-29 CN CN201510363490.6A patent/CN105031958A/en active Pending
Patent Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3332469A (en) * | 1966-09-13 | 1967-07-25 | Rosenblad Corp | Falling film type heat exchanger |
| GB1163364A (en) * | 1967-11-03 | 1969-09-04 | Axel Everhard Rosenblad | Falling Film Evaporator |
| CN2780284Y (en) * | 2005-03-30 | 2006-05-17 | 宜兴市格兰特干燥浓缩设备有限公司 | Improved falling film evaporator |
| WO2014013502A2 (en) * | 2012-07-18 | 2014-01-23 | M/S Raj Process Equipments & Systems Pvt. Ltd. | Non-clog extra long tube falling film evaporation system |
| CN203677967U (en) * | 2014-02-26 | 2014-07-02 | 成都华高生物制品有限公司 | Single-effect falling film concentrator |
| CN204767494U (en) * | 2015-06-29 | 2015-11-18 | 江苏楷益智能科技有限公司 | Falling liquid film formula enrichment facility |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110038315A (en) * | 2019-04-02 | 2019-07-23 | 天津科技大学 | The tube type falling-film vaporising device of a variety of media can be handled simultaneously |
| CN110063405A (en) * | 2019-05-16 | 2019-07-30 | 江苏美德实医疗科技有限公司 | A kind of device and method of industrial efficient batch continuous production collagen |
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| C06 | Publication | ||
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Application publication date: 20151111 |