CN201394370Y - Dual-heating concentration device - Google Patents
Dual-heating concentration device Download PDFInfo
- Publication number
- CN201394370Y CN201394370Y CN2009203032719U CN200920303271U CN201394370Y CN 201394370 Y CN201394370 Y CN 201394370Y CN 2009203032719 U CN2009203032719 U CN 2009203032719U CN 200920303271 U CN200920303271 U CN 200920303271U CN 201394370 Y CN201394370 Y CN 201394370Y
- Authority
- CN
- China
- Prior art keywords
- heater
- evaporimeter
- concentrate
- steam
- thermotank
- 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
Images
Landscapes
- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
Abstract
The utility model discloses a dual-heating concentration device. The device comprises an evaporator (1) and a heater (2); the bottom of the evaporator (1) passes through a return pipe (3) and is connected with the bottom of the heater (2); the upper part of the heater (2) passes through a heat flow pipe (4) and is connected with the middle part of the evaporator (1); and the lower part of the evaporator (1) is provided with an interlayer (5) which is connected with a steam pipe (6) and a condensate water discharge pipe (7). A section of interlayer is added at the lower part of an evaporation barrel and steam is added into the interlayer. After certain concentration is realized in the evaporation, concentrated solution is not required to be taken out of the evaporator and the concentrated solution in the evaporator is heated with steam again, and the concentrated solution is boiled in the evaporator. Two procedures are combined into one procedure, with simple operation. Furthermore, thedevice can improve production efficiency.
Description
Technical field
The utility model relates to a kind of enrichment facility, especially a kind of pair of heating enrichment facility.
Background technology
In the production technology of biological product, often need be placed on boiling obtains in the water liquid to plant and be placed in the enrichment facility and concentrate.Existing enrichment facility is to concentrate about 60 ℃, and the concentrate after concentrating also needs to boil again, needs two procedures, and is cumbersome, also influences production efficiency simultaneously.
The utility model content
The purpose of this utility model is, a kind of pair of heating enrichment facility is provided, and can directly boil concentrate in vaporising device after concentrated finishing, and the synthetic procedure of two procedures is simple to operate, also can enhance productivity.
The technical solution of the utility model: a kind of pair of heating enrichment facility, this device comprises evaporimeter and heater, and the bottom of evaporimeter is connected with the bottom of heater through return duct, and the top of heater is connected with the middle part of evaporimeter through heat flow tube; The Lower Half of evaporimeter is provided with interlayer, and interlayer is connected with drip pipe with steam pipeline.
In above-mentioned two heating enrichment facilities, described evaporimeter comprises the evaporation bucket, and the top of evaporation bucket is provided with vapor outlet port, and the bottom of evaporation bucket is provided with concentrated solution outlet, and concentrated solution outlet is connected with return duct; The middle part of evaporation bucket is provided with concentrate import and 1 or 2 peep hole, and the concentrate import is connected with heat flow tube.
In the aforesaid pair of heating enrichment facility, described heater comprises thermotank, and the thermotank top is provided with charging door, and the thermotank bottom is connected with the concentrate delivery pipe; The side of thermotank is provided with the interface that is connected with heat flow tube with return duct, is provided with the steam sleeve on the thermotank between return duct and the heat flow tube, and the steam sleeve is connected with drip pipe with steam pipeline.
In the aforesaid pair of heating enrichment facility, described steam pipeline, drip pipe and concentrate delivery pipe are provided with valve, and steam pipeline is provided with Pressure gauge.
Compared with prior art, the utility model has increased by one section interlayer in the Lower Half of evaporation bucket, and in interlayer, pass to steam, can be after being evaporated to finite concentration, concentrate need not be taken out from evaporimeter, adopt steam that the concentrate in the evaporimeter is carried out post bake, directly concentrate is boiled in evaporimeter.With the synthetic procedure of two procedures, simple to operate, also can enhance productivity.
Description of drawings
Fig. 1 is a structural representation of the present utility model.
Being labeled as in the accompanying drawing: 1-evaporimeter, 2-heater, 3-return duct, the 4-heat flow tube, 5-interlayer, 6-steam pipeline, 7-drip pipe, 8-evaporate bucket, 9-vapor outlet port, the 10-concentrated solution outlet, the import of 11-concentrate, 12-peep hole, the 13-thermotank, 14-charging door, 15-concentrate delivery pipe, 16-steam sleeve, 17-valve, 18-Pressure gauge.
The specific embodiment
The utility model is described in further detail below in conjunction with drawings and Examples, but not as the foundation of the utility model being done any restriction.
Embodiment.The structure of a kind of pair of heating enrichment facility as shown in Figure 1, the arrow among Fig. 1 is represented the circulating path of concentrate between evaporimeter 1 and heater 2.This device comprises evaporimeter 1 and heater 2, and the effect of heater 2 is that concentrate is heated, and the concentrate after the heating evaporates in evaporimeter 1, and evaporating temperature is about 60 ℃.The bottom of evaporimeter 1 is connected through the bottom of return duct 3 with heater 2, and the top of heater 2 is connected through the middle part of heat flow tube 4 with evaporimeter 1; After concentrate was heated in heater 2, the concentrate of heat entered evaporimeter 1 to rising from heat flow tube 4, and the concentrate that temperature is lower in the evaporimeter 1 flows into heater 2 again from return duct 3, formed the circulation shown in the arrow among Fig. 1.The Lower Half of evaporimeter 1 is provided with interlayer 5, and interlayer 5 is connected with drip pipe 7 with steam pipeline 6.When needs boil concentrate, can open the valve 17 on the steam pipeline 6 that is connected with interlayer 5, by steam the concentrate in the evaporimeter 1 is heated, evaporated liquor is boiled.Evaporimeter 1 comprises evaporation bucket 8, and the top of evaporation bucket 8 is provided with vapor outlet port 9, and the steam that evaporation process produces is discharged.The bottom of evaporation bucket 8 is provided with concentrated solution outlet 10, and concentrated solution outlet 10 is connected with return duct 3; The middle part of evaporation bucket 8 is provided with concentrate import 11 and 1 or 2 peep hole 12, so that the concentrate in the evaporimeter 1 is observed.Concentrate import 11 is connected with heat flow tube 4.Heater 2 comprises thermotank 13, and this thermotank mainly heats evaporation process.Thermotank 13 tops are provided with charging door 14, and the plant liquid that obtains after the plant boiling is added from charging door 14, and thermotank 13 bottoms are connected with concentrate delivery pipe 15; After concentrating end, concentrate is discharged from concentrate delivery pipe 15.Be provided with valve with convenient control at concentrate delivery pipe 15.The side of thermotank 13 is provided with the interface that is connected with heat flow tube 4 with return duct 3, is provided with steam sleeve 16 on the thermotank 13 between return duct 3 and the heat flow tube 4, and steam heats concentrate in steam sleeve 16.Steam sleeve 16 is connected with drip pipe 7 with steam pipeline 6.Steam pipeline 6, drip pipe 7 and concentrate delivery pipe 15 are provided with valve 17, so that control.Steam pipeline 6 is provided with Pressure gauge 18, so that observe steam pressure.
Claims (4)
1. two heating enrichment facility, it is characterized in that: this device comprises evaporimeter (1) and heater (2), the bottom of evaporimeter (1) is connected through the bottom of return duct (3) with heater (2), and the top of heater (2) is connected through the middle part of heat flow tube (4) with evaporimeter (1); The Lower Half of evaporimeter (1) is provided with interlayer (5), and interlayer (5) is connected with drip pipe (7) with steam pipeline (6).
2. according to claim 1 pair of heating enrichment facility, it is characterized in that: described evaporimeter (1) comprises evaporation bucket (8), the top of evaporation bucket (8) is provided with vapor outlet port (9), and the bottom of evaporation bucket (8) is provided with concentrated solution outlet (10), and concentrated solution outlet (10) is connected with return duct (3); The middle part of evaporation bucket (8) is provided with concentrate import (11) and 1 or 2 peep hole (12), and concentrate import (11) is connected with heat flow tube (4).
3. according to claim 2 pair of heating enrichment facility is characterized in that: described heater (2) comprises thermotank (13), and thermotank (13) top is provided with charging door (14), and thermotank (13) bottom is connected with concentrate delivery pipe (15); The side of thermotank (13) is provided with the interface that is connected with heat flow tube (4) with return duct (3), be provided with steam sleeve (16) on the thermotank (13) between return duct (3) and the heat flow tube (4), steam sleeve (16) is connected with drip pipe (7) with steam pipeline (6).
4. according to claim 3 pair of heating enrichment facility is characterized in that: described steam pipeline (6), drip pipe (7) and concentrate delivery pipe (15) are provided with valve (17), and steam pipeline (6) is provided with Pressure gauge (18).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2009203032719U CN201394370Y (en) | 2009-05-18 | 2009-05-18 | Dual-heating concentration device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2009203032719U CN201394370Y (en) | 2009-05-18 | 2009-05-18 | Dual-heating concentration device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN201394370Y true CN201394370Y (en) | 2010-02-03 |
Family
ID=41616858
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2009203032719U Expired - Fee Related CN201394370Y (en) | 2009-05-18 | 2009-05-18 | Dual-heating concentration device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN201394370Y (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106943759A (en) * | 2017-05-17 | 2017-07-14 | 兰溪市同力机械有限公司 | A kind of waste acid recovery system |
-
2009
- 2009-05-18 CN CN2009203032719U patent/CN201394370Y/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106943759A (en) * | 2017-05-17 | 2017-07-14 | 兰溪市同力机械有限公司 | A kind of waste acid recovery system |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN105327518B (en) | The concentration systems and method of a kind of pentanediamine | |
| CN201921534U (en) | Low-temperature evaporation concentration device | |
| CN104922921B (en) | A kind of self-loopa MVR thermo-compression evaporation systems | |
| CN204874480U (en) | A distillation heating device for making wine | |
| CN202951265U (en) | Efficient evaporating crystallizer | |
| CN201394370Y (en) | Dual-heating concentration device | |
| CN203886205U (en) | Low-temperature concentrating device | |
| CN205627127U (en) | MVR triple -effect evaporator | |
| CN102319516A (en) | Low-temperature vacuum thickener | |
| CN208905999U (en) | A kind of steam collection device for Producing medicinal herbs | |
| CN203281053U (en) | Quadruple-effect downstream falling-film evaporator for preparation of inositol | |
| CN110081596A (en) | A kind of bittern bromine heat-exchanger rig | |
| CN205815139U (en) | A kind of circulating aluminum pipe vaporizer | |
| CN201415068Y (en) | Device for extracting and concentrating effective ingredient of traditional Chinese medicine | |
| CN101612487A (en) | The extraction of effective components of Chinese medicinal and concentrator and extraction and method for concentration | |
| CN201454559U (en) | Distillation and purification device for solvents | |
| CN204767477U (en) | Medicine concentrator | |
| CN206138766U (en) | Food detects distillation plant | |
| CN204684685U (en) | A kind of cryogenic vacuum Chinese medicinal concentration equipment | |
| CN204159049U (en) | A kind of quadruple effect vacuum falling film evaporimeter with vapour-recovery unit | |
| CN207507037U (en) | One Plant Extracts material enrichment facility | |
| CN207445624U (en) | A kind of energy-saving distilling enrichment facility for pharmacy | |
| CN103083928A (en) | Novel heating evaporator | |
| CN207119155U (en) | Multiple-effect evaporation concentration systems | |
| CN202802822U (en) | High-efficiency Chinese medicament evaporation extraction device |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C17 | Cessation of patent right | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20100203 Termination date: 20140518 |