CN201848110U - Novel vacuum concentrator - Google Patents
Novel vacuum concentrator Download PDFInfo
- Publication number
- CN201848110U CN201848110U CN200920175272XU CN200920175272U CN201848110U CN 201848110 U CN201848110 U CN 201848110U CN 200920175272X U CN200920175272X U CN 200920175272XU CN 200920175272 U CN200920175272 U CN 200920175272U CN 201848110 U CN201848110 U CN 201848110U
- Authority
- CN
- China
- Prior art keywords
- vaporization chamber
- vacuum concentrator
- novel vacuum
- semiaxis
- feature
- 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
- 238000001704 evaporation Methods 0.000 claims abstract description 12
- 239000000463 material Substances 0.000 claims abstract description 10
- 238000009834 vaporization Methods 0.000 claims description 35
- 230000008016 vaporization Effects 0.000 claims description 35
- 230000005540 biological transmission Effects 0.000 claims description 5
- 230000007306 turnover Effects 0.000 claims description 2
- 239000000919 ceramic Substances 0.000 claims 1
- 239000007769 metal material Substances 0.000 claims 1
- 238000009987 spinning Methods 0.000 claims 1
- 239000007788 liquid Substances 0.000 abstract description 11
- 239000012141 concentrate Substances 0.000 abstract description 5
- 230000008020 evaporation Effects 0.000 abstract description 5
- 238000004939 coking Methods 0.000 abstract description 3
- 238000005265 energy consumption Methods 0.000 abstract description 3
- 238000004519 manufacturing process Methods 0.000 abstract description 3
- 239000000126 substance Substances 0.000 abstract description 3
- 238000010438 heat treatment Methods 0.000 abstract description 2
- 238000005406 washing Methods 0.000 abstract 1
- 238000002425 crystallisation Methods 0.000 description 4
- 230000008025 crystallization Effects 0.000 description 4
- 239000010408 film Substances 0.000 description 4
- 238000012423 maintenance Methods 0.000 description 3
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 2
- 239000013078 crystal Substances 0.000 description 2
- 239000006052 feed supplement Substances 0.000 description 2
- 239000012530 fluid Substances 0.000 description 2
- BGOFCVIGEYGEOF-UJPOAAIJSA-N helicin Chemical compound O[C@@H]1[C@@H](O)[C@H](O)[C@@H](CO)O[C@H]1OC1=CC=CC=C1C=O BGOFCVIGEYGEOF-UJPOAAIJSA-N 0.000 description 2
- 230000008719 thickening Effects 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 1
- 239000004743 Polypropylene Substances 0.000 description 1
- 229910000831 Steel Inorganic materials 0.000 description 1
- 230000006978 adaptation Effects 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 230000015556 catabolic process Effects 0.000 description 1
- 238000004140 cleaning Methods 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 229910052802 copper Inorganic materials 0.000 description 1
- 239000010949 copper Substances 0.000 description 1
- 238000009826 distribution Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000011552 falling film Substances 0.000 description 1
- 239000011521 glass Substances 0.000 description 1
- 230000002779 inactivation Effects 0.000 description 1
- 229910052742 iron Inorganic materials 0.000 description 1
- 239000012528 membrane Substances 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 229910052755 nonmetal Inorganic materials 0.000 description 1
- -1 polypropylene Polymers 0.000 description 1
- 229920001155 polypropylene Polymers 0.000 description 1
- 230000001105 regulatory effect Effects 0.000 description 1
- 229910001220 stainless steel Inorganic materials 0.000 description 1
- 239000010935 stainless steel Substances 0.000 description 1
- 230000003068 static effect Effects 0.000 description 1
- 239000010959 steel Substances 0.000 description 1
Images
Landscapes
- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
Abstract
The utility model relates to a novel vacuum concentrator. An evaporation device is of a rotary spherical (or a spheroidicity) container which is formed by an evaporation chamber and a jacket. The heating area of the concentrator and the area of a concentrate liquid film are large, so the concentration speed is fast; and the inner wall of the evaporation chamber is smooth and is free from dead corners, the withdrawn liquid film is thin and uniform, and the heat conduction is uniform, so no shell clingage and coking phenomenon exist, and the novel vacuum concentrator is particularly suitable for the heat-sensitive substances and the materials which are easy to be crystallized. The concentrator has a simple structure, is easy to manufacture and repair, and has the advantages of low energy consumption, high concentration efficiency, convenience in washing and the like.
Description
Technical field
The utility model relates to a kind of novel vacuum concentrator, is applicable to the concentrating of material of heat-sensitive materials and easily crystallization, belongs to the plant equipment field.
Technical background
Vacuum concentrator is extensively in chemistry, pharmacy and Applications in Food Industry, and existing at present polytype vacuum concentrating apparatus as " falling film condenser ", has some vertical channels in its vaporization chamber, and the heated liquid evaporation in the passage of flowing through reaches concentrated purpose.And for example " rotating cage inspissator " is a rotating cage of being made up of some hollow pipes in its vaporization chamber, logical hot water or steam in the pipe, and the rotating cage rotation makes the heated liquid evaporation on the tube-surface, reaches concentrated purpose.But existing these inspissators exist that to concentrate area little, and heat conduction is inhomogeneous, makes the crystallization that concentrates be prone to the phenomenon of sticking wall and coking, causes the heat-sensitive substance inactivation, causes thickening efficiency to descend.And since these inspissator complex structures, easy break-down in the use, its manufacturing and maintenance cost height, energy consumption is big, not easy cleaning.
The utility model content
At the shortcoming that existing vacuum concentrator exists, the utility model has designed a kind of vacuum concentrator that is applicable to the material of heat-sensitive substance and easy crystallization.
The utility model solves the problems of the technologies described above the technical scheme that is adopted: a kind of novel vacuum concentrator, and it is by feed pipe, vaporising device, power set and transmission device are formed.It is characterized in that: vaporising device.
Described vaporising device is the rotatable sphere or the elliptical container that are made of vaporization chamber and chuck, the inwall of vaporization chamber is evaporating surface of the present invention, its inwall is the evaporating surface at smooth no dead angle, visor is housed on the vaporization chamber, can one or morely concentrate situation, feed supplement at any time so that observe material; Spiral flow deflector is housed in the chuck.
Described flow deflector is installed in the chuck, is one group of spiral helicine plate, and spiral angle is the 10-20 degree, is preferably 15 degree (shown in figure two), and the inboard is fixed with the vaporization chamber outer wall respectively.Heat transfer medium flows is line in the shape of a spiral, and the fluid turbulent degree strengthens, and helps heat exchange, heat-conducting medium was evenly distributed reduced stagnant area and dead band, improve heat transfer efficiency, can increase the intensity of vaporization chamber again, reduce the wall thickness of vaporization chamber, further improve heat transfer efficiency.
Advantage of the present utility model is as follows: 1, the area of heating surface (area) (HS and concentrated liquid film is very big, so the speed of concentrating is fast; 2, inner wall smooth, no dead angle, the liquid film of pulling out is thin and even, adds that heat conduction is even, so do not have sticking wall and coking phenomenon; 3, in the vaporization chamber rotary course, the material of its interior dress does not rotate thereupon, but keeps static relatively, thereby the crystal formation of crystal is good especially, can not stop up inspissator, is specially adapted to the material of heat-sensitive materials and easy crystallization; 4, the vaporization chamber inwall is evaporating surface, no rotor in the vaporization chamber, and devices such as heat pipe and agitator, thereby be easy to manufacturing, maintenance and maintenance and with low cost; 5, thickening efficiency height, energy consumption is low; 6, be convenient to clean.
Description of drawings
Fig. 1 is the structure cutaway view of vacuum concentrator of the present utility model;
Fig. 2 is the cutaway view of the flow deflector of vacuum concentrator of the present utility model.
The specific embodiment
Below in conjunction with accompanying drawing embodiment the utility model is done and to be described in further detail.
The utility model is a kind of novel vacuum concentrator, and it is by feed pipe (1), vaporising device (2), and power set (5) and transmission device (8) are formed.It is characterized in that: vaporising device is the rotatable sphere or the elliptical container that are made of vaporization chamber (6) and chuck (3), and the inwall of vaporization chamber (6) is evaporating surface of the present invention; Spiral flow deflector (9) is housed in the chuck (3).
The utility model is shown in figure one, vaporising device (2) is the container that is made of vaporization chamber (6) and chuck (3), it is shaped as spheroidal or oval spherical, and available metal (as stainless steel, steel, iron, copper etc.) or nonmetal (as pottery, glass, polypropylene, poly-tetrafluoro etc.) are made.Inwall requires smooth, can polish or serve as a contrast pottery, poly-tetrafluoro etc.When container rotated, its inwall was the evaporating surface at smooth no dead angle; Vaporization chamber is equipped with visor on (6), can one or morely concentrate situation, feed supplement at any time so that observe material.The stocking volume of vaporization chamber (6) is 0.01～20 cubic metre.
Transmission device (8) is made up of semiaxis (7) and semiaxis (14), is fixed in vaporising device (2) two ends and is contained on the support (15) of power set (5).The heat pipe (11) of turnover heat-conducting medium (constant-temperature hot water, steam, deep fat etc.) is housed in the semiaxis (14), and an end is connected with chuck (3); Vacuum tube (10) and feed pipe (1) then are housed in the semiaxis (7), and the vapor collection pipe (16) that vacuum tube (10) connects is drawn cooling with steam with vacuum mode and is reclaimed or discharge, and charging then realizes by the feed pipe (1) of feeding device.
Power set (5) are made up of motor, reductor (4) and support (15), and rotating speed is 5-20 rev/min, and the CD-ROM drive motor distribution installs frequency converter additional, accomplish that soft start is to avoid starting the impulsive force and the demands of regulating the different concentrated media of rotating speed adaptation of starting stage.
Flow deflector (9) is installed in the chuck (3), is one group of spiral helicine plate, and spiral angle is the 10-20 degree, is preferably 15 degree (shown in figure two), and the inboard is fixed with vaporization chamber (6) outer wall respectively.Heat transfer medium flows is line in the shape of a spiral, and the fluid turbulent degree strengthens, and helps heat exchange, heat-conducting medium was evenly distributed reduced stagnant area and dead band, improve heat transfer efficiency, can increase the intensity of vaporization chamber (6) again, reduce the wall thickness of vaporization chamber (6), further improve heat transfer efficiency.
Operation principle of the present utility model is, by power set (5) jack shafts (7), driving vaporization chamber (6) and chuck (3) rotates, heat-conducting medium enters chuck (3) through heat pipe simultaneously, to vaporization chamber (6) is heated, the inwall of vaporization chamber (6) is evaporating surface, after liquid to be concentrated enters vaporization chamber (6), rotation along with vaporization chamber (6), liquid is constantly pulled out the liquid film of the uniform concentrated liquid of a layer thickness in vaporization chamber (6) inwall top, under heat effect, the moisture content in liquid film vaporization is rapidly taken away by vacuum by upright vapor collection pipe (16); In the process of constantly membrane and vaporization, the solution to be concentrated body in the vaporization chamber (6) is concentrated gradually.
Claims (6)
1. a vacuum concentrator is by feed pipe (1), vaporising device (2), power set (5), and transmission device (8) is formed, it is characterized in that: vaporising device is the rotatable sphere or the elliptical container that are made of vaporization chamber (6) and chuck (3), and the inwall of vaporization chamber (6) is evaporating surface of the present invention; Transmission device is made up of semiaxis (7) and semiaxis (14); Spiral flow deflector (9) is housed in the chuck (3).
2. novel vacuum concentrator according to claim 1, its feature is the surface of burnishing surface or ceramic, the poly-tetrafluoro of lining at the inwall of said vaporization chamber (6).
3. novel vacuum concentrator according to claim 1, its feature wherein is equipped with vacuum tube (10), feed pipe (1) in a semiaxis at said two fixing semiaxis of vaporization chamber (7), and another semiaxis is equipped with heat medium turnover pipe (11).
4. novel vacuum concentrator according to claim 1 and 2, its feature are equipped with drain hole (12) and observation panel (13) on said vaporization chamber (6).
5. novel vacuum concentrator according to claim 1, its feature can be made with metal material or nonmetallic materials at said vaporization chamber (6).
6. novel vacuum concentrator according to claim 1 and 2, its feature is one group of spiral-shaped thin plate at said spinning disk (9), and spiral angle is the 10-20 degree, and inboard and vaporization chamber (6) outer wall is fixed together.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN200920175272XU CN201848110U (en) | 2009-09-03 | 2009-09-03 | Novel vacuum concentrator |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN200920175272XU CN201848110U (en) | 2009-09-03 | 2009-09-03 | Novel vacuum concentrator |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN201848110U true CN201848110U (en) | 2011-06-01 |
Family
ID=44090525
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN200920175272XU Expired - Fee Related CN201848110U (en) | 2009-09-03 | 2009-09-03 | Novel vacuum concentrator |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN201848110U (en) |
-
2009
- 2009-09-03 CN CN200920175272XU patent/CN201848110U/en not_active Expired - Fee Related
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN101693148A (en) | Novel vacuum concentrator | |
| AU2008213550A1 (en) | Microwave rotary film concentrator | |
| JP3249540U (en) | Emulsion cooling device | |
| CN111097187A (en) | A new type of crystallization kettle that can improve the efficiency of evaporative crystallization | |
| CN204090906U (en) | A kind of antiseepage Yoghourt fermentation tank | |
| CN114392572A (en) | A solvent separation device for plant extraction mixture | |
| CN214181831U (en) | Distillation purification device of spandex production usefulness | |
| CN201848110U (en) | Novel vacuum concentrator | |
| CN213100902U (en) | Novel crystallization kettle capable of improving evaporation crystallization efficiency | |
| CN207035579U (en) | Efficient rotary pipe type heat transfer evaporator | |
| CN207095341U (en) | A kind of good jacketed type exchanger of heat exchange property | |
| CN206392030U (en) | One kind energy-conservation reactor system | |
| CN210612903U (en) | Novel ball-type concentrator is used in medicine subsides production | |
| CN201026400Y (en) | Microwave rotating film concentrator | |
| CN101182458B (en) | Dynamic heat pipe stirring bioreactor for various biological reactions | |
| CN209679520U (en) | Vaporising device is used in a kind of concentration of chemical industry | |
| CN217012578U (en) | Flash distillation device for condensed milk | |
| CN206414780U (en) | a thin film evaporator | |
| CN104001466A (en) | Temperature-controllable refining agent reaction kettle | |
| CN205730441U (en) | A kind of crystallization kettle | |
| CN103894133B (en) | A kind of printing and dyeing chemical industry reaction unit | |
| CN207025261U (en) | A kind of textile industry low boiling softener raw material prilling granulator | |
| CN109386994A (en) | Efficient rotary pipe type heat transfer evaporator and heat-exchange method | |
| CN208927623U (en) | Rectifier unit | |
| CN102240459A (en) | Solution concentrator unit |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| DD01 | Delivery of document by public notice |
Addressee: Yang Xusheng Document name: First amendment notice |
|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20110601 Termination date: 20170903 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |