CN208660388U - A kind of oral solution dual-effect concentrator of high production capacity - Google Patents
A kind of oral solution dual-effect concentrator of high production capacity Download PDFInfo
- Publication number
- CN208660388U CN208660388U CN201820941111.6U CN201820941111U CN208660388U CN 208660388 U CN208660388 U CN 208660388U CN 201820941111 U CN201820941111 U CN 201820941111U CN 208660388 U CN208660388 U CN 208660388U
- Authority
- CN
- China
- Prior art keywords
- effect
- evaporator
- heater
- gas
- fixedly mounted
- 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
Landscapes
- Devices For Medical Bathing And Washing (AREA)
Abstract
The utility model discloses a kind of oral solution dual-effect concentrators of high production capacity, including two effect heaters, 2nd effect evaporator, condenser, receive flow container, one effect heater and 1st effective evaporator, in the top sidewall of the one effect heater be installed communicating pipe, the other end of communicating pipe and the inside of 1st effective evaporator connect, the second discharge port is fixedly mounted in the bottom of the 1st effective evaporator, second discharge port of the 1st effective evaporator bottom is connected to by the second passage with the bottom sidewall of the effect heater, the first gas-liquid separator is fixedly mounted in the outside of the 1st effective evaporator, the steam (vapor) outlet of the 1st effective evaporator is connect by gas-guide tube with the overhead vapor entrance of two effect heaters, in the top sidewall of the two effects heater be installed communicating pipe, the other end of the communicating pipe is connect with the inside of the 2nd effect evaporator, the high production capacity Oral solution dual-effect concentrator structure is simple, makes to have conveniently, and heat utilization rate is high, with short production cycle, is worthy to be popularized.
Description
Technical field
The utility model relates to a kind of inspissator, the oral solution dual-effect concentrator of specifically a kind of high production capacity.
Background technique
Dual-effect concentrator is using two effects while evaporating, and secondary steam is fully used and not only saves the investment of boiler, but also
Energy saving, energy consumption reduce by 50% compared with single-effect concentrator；Dual-effect concentrator uses external heat Natural Circulation and negative pressure of vacuum
Mode, evaporation rate is fast, and cocnentration factor is great.
The shortcomings that existing purpose double-action condenser, is: using recirculating certainly, causing the cycle rate of medical fluid low, evaporation capacity
It is small, meanwhile, the processing efficiency of medical fluid is lower, and heat distributes fastly during heating, and cause heating uneven, meanwhile, it is evaporating
The condensed water generated on evaporator side wall in the process falls, and discharge can not huge profit use.
Utility model content
The purpose of this utility model is to provide a kind of oral solution dual-effect concentrators of high production capacity, to solve above-mentioned background skill
The problem of being proposed in art.
To achieve the above object, the utility model provides the following technical solutions:
A kind of oral solution dual-effect concentrator of high production capacity, including two effect heaters, 2nd effect evaporator, condenser, receive flow container,
Circulating pump, an effect heater and 1st effective evaporator are installed communicating pipe in the top sidewall of the one effect heater, communicating pipe it is another
One end and the inside of 1st effective evaporator connect, and the second discharge port is fixedly mounted in the bottom of the 1st effective evaporator, and an effect is steamed
Second discharge port of hair device bottom is connected to by the second passage with the bottom sidewall of the effect heater, the effect evaporation
The first gas-liquid separator is fixedly mounted in the outside of device, and the steam (vapor) outlet of the 1st effective evaporator passes through gas-guide tube and two effect heaters
Overhead vapor entrance connection, it is described two effect heater top sidewall on install communicating pipe, the other end of the communicating pipe with
The inside of the 2nd effect evaporator connects, and the second discharge port, the two effects evaporation is fixedly mounted in the bottom of the 2nd effect evaporator
Second discharge port of device is connected to by the second passage with the bottom sidewall of the two effects heater, outside the 2nd effect evaporator
The first gas-liquid separator is fixedly mounted in side, and the steam (vapor) outlet of the 2nd effect evaporator is connected by the air inlet of gas-guide tube and condenser
Logical, the condenser is fixedly mounted on the top for receiving flow container, and the outside for receiving flow container is equipped with the second gas-liquid separator, described
The import of second gas-liquid separator is connect with the outlet of the condenser, the liquid-phase outlet of second gas-liquid separator with it is described
Flow container connection is received, the gaseous phase outlet of second gas-liquid separator is connect with the air inlet of the condenser.
As a further solution of the present invention: the first discharge port is fixedly mounted in the bottom of an effect heater, an effect adds
First discharge port of hot device bottom is connected to by the first passage with the first discharge port of the two effects heater, and the first guide
Dehvery pump is fixedly mounted on pipe, is fixedly mounted and recycles on an effect heater and the second passage of the 1st effective evaporator
Pump.
Second guide of two the effects heater and the 2nd effect evaporator as a further solution of the present invention,
Circulating pump is fixedly mounted on pipe.
The structure phase of the 1st effective evaporator and the 2nd effect evaporator as a further solution of the present invention,
Together, the 1st effective evaporator and the 2nd effect evaporator are made of steam port, liner, shell and helicoidal stream coil pipe, described
Liner is fixedly mounted in the inside of shell, and insulating layer, the steam port and the second discharging are formed between the shell and the liner
Mouth is connected to the liner, and the steam port is connected to by conduit with the inlet end of first gas-liquid separator, and spiral is steamed
Vapour coil pipe is fixedly mounted in the insulating layer, the gas phase of the bottom end of the helicoidal stream coil pipe and first gas-liquid separator
Lower water valve is fixedly mounted in outlet connection, the liquid-phase outlet of first gas-liquid separator, and the top of the helicoidal stream coil pipe is passed through
It wears to the outside of the shell.
Thermal insulation material, the thermal insulation material are filled in the insulating layer as a further solution of the present invention,
For mineral wool or one kind of rock wool.
Compared with prior art, the utility model has the beneficial effects that
This utility structure is simple, easy to use, and compared with conventional evaporator, this practical evaporator is double-layer structure, shell
The insulating layer for being filled with thermal insulation material is formed between body and liner, and helicoidal stream coil pipe is fixedly mounted in insulating layer, by evaporating
The steam that device generates heats insulating layer, to improve utilization efficiency of heat energy, reaches good energy-saving effect, and make to evaporate
Device remains constant temperature level, slows down radiating rate, reduces heat losses, accelerates drug evaporation rate, dense so as to shorten drug
The contracting period.
Detailed description of the invention
Fig. 1 is the structural schematic diagram of the oral solution dual-effect concentrator of high production capacity.
Fig. 2 is the structural schematic diagram of 2nd effect evaporator in the oral solution dual-effect concentrator of high production capacity.
In figure: the first gas-liquid separator 1, two imitates heater 2, communicating pipe 3,2nd effect evaporator 4, condenser 5, the second gas-liquid
Separator 6 receives flow container 7, circulating pump 8, the effect of dehvery pump 9, one heater 10,1st effective evaporator 11, steam port 12, liner 13, protects
Warm layer 14, shell 15, helicoidal stream coil pipe 16, the first passage 17, the first discharge port 18, the second discharge port 19 and the second guide
Pipe 20.
Specific embodiment
The following will be combined with the drawings in the embodiments of the present invention, carries out the technical scheme in the embodiment of the utility model
Clearly and completely describe, it is clear that the described embodiments are only a part of the embodiments of the utility model, rather than whole
Embodiment.Based on the embodiments of the present invention, those of ordinary skill in the art are without making creative work
Every other embodiment obtained, fall within the protection scope of the utility model.
Please refer to Fig. 1~2, in the utility model embodiment, a kind of oral solution dual-effect concentrator of high production capacity, including first
Gas-liquid separator 1, two imitate heater 2, communicating pipe 3,2nd effect evaporator 4, condenser 5, the second gas-liquid separator 6, receive flow container 7,
Circulating pump 8, dehvery pump 9, one imitate heater 10,1st effective evaporator 11, steam port 12, liner 13, insulating layer 14, shell 15, spiral shell
Steam pipe coil 16, the first passage 17, the first discharge port 18, the second discharge port 19 and the second passage 20 are revolved, an effect adds
Communicating pipe 3 is installed in the top sidewall of hot device 10, the other end of communicating pipe 3 is connect with the inside of 1st effective evaporator 11, and described one
The bottom for imitating evaporator 11 is fixedly mounted the second discharge port 19, and the second discharge port 19 of 11 bottom of 1st effective evaporator passes through the
Two passages 20 are connected to the bottom sidewall of the effect heater 10, and the outside of the 1st effective evaporator 11 is fixedly mounted first
The steam (vapor) outlet of gas-liquid separator 1, the 1st effective evaporator 11 is connected by the overhead vapor entrance of gas-guide tube and two effect heaters 2
It connects, is installed communicating pipe 3 in the top sidewall of the two effects heater 2, the other end and the 2nd effect evaporator of the communicating pipe 3
The second discharge port 19 is fixedly mounted in 4 inside connection, the bottom of the 2nd effect evaporator 4, and the second of the 2nd effect evaporator 4 goes out
Material mouth 19 is connected to by the second passage 20 with the bottom sidewall of the two effects heater 2, and the outside of the 2nd effect evaporator 4 is solid
Dingan County fills the first gas-liquid separator 1, and the steam (vapor) outlet of the 2nd effect evaporator 4 is connected by the air inlet of gas-guide tube and condenser 5
Logical, the condenser 5 is fixedly mounted on the top for receiving flow container 7, and the outside for receiving flow container 7 is equipped with the second gas-liquid separator 6,
The import of second gas-liquid separator 6 is connect with the outlet of the condenser 5, and the liquid phase of second gas-liquid separator 6 goes out
Mouth is connect with the receipts flow container 7, and the gaseous phase outlet of second gas-liquid separator 6 is connect with the air inlet of the condenser 5, institute
The first discharge port 18 is fixedly mounted in the bottom for stating an effect heater 10, and the first discharge port 18 of effect 10 bottom of heater passes through the
One passage 17 is connected to the first discharge port 18 of the two effects heater 2, and dehvery pump is fixedly mounted on the first passage 17
9, described one imitates fixed installation circulating pump 8 on the second passage 20 of heater 10 and the 1st effective evaporator 11；Two effect
Circulating pump 8 is fixedly mounted on second passage 20 of heater 2 and the 2nd effect evaporator 4；The 1st effective evaporator 11 and institute
The structure for stating 2nd effect evaporator 4 is identical, the 1st effective evaporator 11 and the 2nd effect evaporator 4 by steam port 12, liner 13,
Shell 15 and helicoidal stream coil pipe 16 are constituted, and the inside of the shell 15 is fixedly mounted liner 13, the shell 15 with it is described interior
Insulating layer 14 is formed between gallbladder 13, the steam port 12 and the second discharge port 19 are connected to the liner 13, the steam port
12 are connected to by conduit with the inlet end of first gas-liquid separator 1, and helicoidal stream coil pipe 16 is fixedly mounted on the heat preservation
In layer 14, the bottom end of the helicoidal stream coil pipe 16 is connect with the gaseous phase outlet of first gas-liquid separator 1, first gas
Lower water valve is fixedly mounted in the liquid-phase outlet of liquid/gas separator 1, and the top of the helicoidal stream coil pipe 16 is through to the shell 15
Outside, the insulating layer 14 is interior to be filled with thermal insulation material, and the thermal insulation material is one kind of mineral wool or rock wool；In use, high
Warm steam is passed through by an effect heater 10, and is heated to drug, and the aqueous solvent in drug is heated by an effect heater 10
Evaporation, which produces, afterwards forms secondary steam, and secondary steam is entered in 1st effective evaporator 11 by communicating pipe 3, the drug in an effect heater 10
Its concentration is greater than the drug concentration in 1st effective evaporator 11 after evaporating, therefore the drug in 1st effective evaporator 11 passes through the second guide
Flowing in 20 Xiang Yixiao heater 10 of pipe, to make 10 He of an effect heater to the principle that high concentration is spread according to low concentration drug
Drug progress self-loopa concentration in 1st effective evaporator 11, the bottom deposit that drug concentrate constantly imitates heater 10 one, from
And realize primary concentration, circulating pump 8 can speed up the height in the low concentration medical fluid Xiang Yixiao heater 10 in 1st effective evaporator 11
Concentration liquid diffusion velocity so that forced circulation is changed into self-loopa, therefore greatly improves medical fluid evaporation rate, and primary concentration produces
Raw secondary steam is entered in helicoidal stream coil pipe 16 by the first gas-liquid separator 1, so that insulating layer 14 is heated, thus
It is consistent 13 internal and external temperature of liner of 1st effective evaporator 11, slows down the radiating rate of 1st effective evaporator 11, is improved secondary
Steam thermal energy utilization efficiency, secondary steam is passed through in two effect heaters 2 after being released by helicoidal stream coil pipe 16, while passing through conveying
Pump 9 by one imitate heater 10 in primary concentration drug be pumped into two effect heaters 2, and to two effect heaters 2 in drug into
Row reheating, the drug after heating are further concentrated by evaporation in 2nd effect evaporator 4, and output drug concentrate, secondary to add
The steam generated after heat equally enters helicoidal stream coil pipe 16 by the first gas-liquid separator 1 and to the heat preservation in 2nd effect evaporator 4
Layer 14 carries out heating and thermal insulation, to further increase utilization efficiency of heat energy, the steam that 2nd effect evaporator 4 generates is cold by condenser 5
Coalescence is collected condensed water by receipts flow container 7, to complete concentration operation.
The working principle of the utility model is:
In use, high-temperature steam is passed through by an effect heater 10, and drug is heated, the aqueous solvent in drug passes through
Evaporation, which produces, after one effect heater 10 heats forms secondary steam, and secondary steam is entered in 1st effective evaporator 11 by communicating pipe 3, an effect
Drug in heater 10 its concentration after evaporating is greater than the drug concentration in 1st effective evaporator 11, therefore in 1st effective evaporator 11
Drug is by flowing in 20 Xiang Yixiao heater 10 of the second passage, thus the principle spread according to low concentration drug to high concentration
The drug in an effect heater 10 and 1st effective evaporator 11 is set to carry out self-loopa concentration, drug concentrate constantly imitates heater one
10 bottom deposit, to realize primary concentration, circulating pump 8 can speed up the low concentration medical fluid Xiang Yixiao in 1st effective evaporator 11
High concentration medical fluid diffusion velocity in heater 10 so that forced circulation is changed into self-loopa, therefore greatly improves medical fluid evaporation
Speed, the secondary steam that primary concentration generates is entered in helicoidal stream coil pipe 16 by the first gas-liquid separator 1, thus to insulating layer
14 are heated, so that 13 internal and external temperature of liner of 1st effective evaporator 11 be made to be consistent, slow down dissipating for 1st effective evaporator 11
Thermal velocity, improves secondary steam utilization efficiency of heat energy, and secondary steam is passed through two effect heaters 2 after being released by helicoidal stream coil pipe 16
In, while the primary concentration drug in heater 10 is imitated for one by dehvery pump 9 and is pumped into two effect heaters 2, and two effects are added
Drug in hot device 2 carries out reheating, and the drug after heating is further concentrated by evaporation in 2nd effect evaporator 4, and output medicine
Concentrate is savored, the steam generated after reheating equally enters helicoidal stream coil pipe 16 by the first gas-liquid separator 1 and imitates to two
Insulating layer 14 in evaporator 4 carries out heating and thermal insulation, so that utilization efficiency of heat energy is further increased, what 2nd effect evaporator 4 generated
Steam is condensed by condenser 5 and is collected by receipts flow container 7 to condensed water, to complete concentration operation.
Although the utility model is described in detail with reference to the foregoing embodiments, come for those skilled in the art
Say, it is still possible to modify the technical solutions described in the foregoing embodiments, or to part of technical characteristic into
Row equivalent replacement, within the spirit and principle of the utility model, any modification, equivalent replacement, improvement and so on should all
It is included within the scope of protection of this utility model.
Claims (5)
1. a kind of oral solution dual-effect concentrator of high production capacity, including two effects heater (2), 2nd effect evaporator (4), condenser (5),
Receive flow container (7), circulating pump (8), effect heater (10) and 1st effective evaporator (11), which is characterized in that the effect heater
(10) communicating pipe (3) are installed in top sidewall, the other end of communicating pipe (3) is connect with the inside of 1st effective evaporator (11), institute
The second discharge port (19) are fixedly mounted in the bottom for stating 1st effective evaporator (11), the second discharging of 1st effective evaporator (11) bottom
Mouth (19) is connected to by the second passage (20) with the bottom sidewall of effect heater (10), the 1st effective evaporator (11)
Outside the first gas-liquid separator (1) is fixedly mounted, the steam (vapor) outlet of the 1st effective evaporator (11) is imitated by gas-guide tube with two
The overhead vapor entrance of heater (2) connects, and installs communicating pipe (3) in the top sidewall of two effect heater (2), the company
The other end of siphunculus (3) is connect with the inside of the 2nd effect evaporator (4), and the bottom of the 2nd effect evaporator (4) is fixedly mounted
The second discharge port (19) of second discharge port (19), the 2nd effect evaporator (4) passes through the second passage (20) and two effect
The bottom sidewall of heater (2) is connected to, and the first gas-liquid separator (1) is fixedly mounted in the outside of the 2nd effect evaporator (4), described
The steam (vapor) outlet of 2nd effect evaporator (4) is connected to by gas-guide tube with the air inlet of condenser (5), the fixed peace of the condenser (5)
Mounted in the top for receiving flow container (7), the outside for receiving flow container (7) is equipped with the second gas-liquid separator of institute (6), second gas-liquid point
Import from device (6) is connect with the outlet of the condenser (5), the liquid-phase outlet of second gas-liquid separator (6) with it is described
Flow container (7) connection is received, the gaseous phase outlet of second gas-liquid separator (6) is connect with the air inlet of the condenser (5).
2. the oral solution dual-effect concentrator of high production capacity according to claim 1, which is characterized in that the effect heater
(10) the first discharge port (18) are fixedly mounted in bottom, and first discharge port (18) of effect heater (10) bottom is led by first
Expects pipe (17) is connected to the first discharge port (18) of two effect heater (2), and is fixedly mounted on the first passage (17) defeated
Material pump (9), effect heater (10) are recycled with fixed installation on second passage (20) of the 1st effective evaporator (11)
It pumps (8).
3. the oral solution dual-effect concentrator of high production capacity according to claim 2, which is characterized in that the two effects heater
(2) circulating pump (8) are fixedly mounted on second passage (20) of the 2nd effect evaporator (4).
4. the oral solution dual-effect concentrator of high production capacity according to claim 1, which is characterized in that the 1st effective evaporator
(11) identical with the structure of the 2nd effect evaporator (4), the 1st effective evaporator (11) and the 2nd effect evaporator (4) are by steaming
Steam ports (12), liner (13), shell (15) and helicoidal stream coil pipe (16) are constituted, in the inside fixed installation of the shell (15)
Gallbladder (13) forms insulating layer (14) between the shell (15) and the liner (13), the steam port (12) and the second discharging
Mouthful (19) be connected tos with the liner (13), the steam port (12) by conduit and first gas-liquid separator (1) into
The connection of gas end, helicoidal stream coil pipe (16) are fixedly mounted in the insulating layer (14), the bottom of the helicoidal stream coil pipe (16)
End is connect with the gaseous phase outlet of first gas-liquid separator (1), the fixed peace of the liquid-phase outlet of first gas-liquid separator (1)
Water valve is loaded, the top of the helicoidal stream coil pipe (16) is through to the outside of the shell (15).
5. the oral solution dual-effect concentrator of high production capacity according to claim 4, which is characterized in that in the insulating layer (14)
Filled with thermal insulation material, the thermal insulation material is one kind of mineral wool or rock wool.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201820941111.6U CN208660388U (en) | 2018-06-19 | 2018-06-19 | A kind of oral solution dual-effect concentrator of high production capacity |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201820941111.6U CN208660388U (en) | 2018-06-19 | 2018-06-19 | A kind of oral solution dual-effect concentrator of high production capacity |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN208660388U true CN208660388U (en) | 2019-03-29 |
Family
ID=65824513
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201820941111.6U Active CN208660388U (en) | 2018-06-19 | 2018-06-19 | A kind of oral solution dual-effect concentrator of high production capacity |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN208660388U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110639217A (en) * | 2019-10-10 | 2020-01-03 | 赵洁 | Triple-effect evaporator |
-
2018
- 2018-06-19 CN CN201820941111.6U patent/CN208660388U/en active Active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110639217A (en) * | 2019-10-10 | 2020-01-03 | 赵洁 | Triple-effect evaporator |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN103768808B (en) | Some vapor recompression evaporation concentration system and method | |
| CN103951005B (en) | The more technology coupling seawater desalination plants of zero-emission and its method | |
| CN106196727B (en) | A kind of heat pump system and its operation method | |
| CN104922921B (en) | A kind of self-loopa MVR thermo-compression evaporation systems | |
| CN207507042U (en) | Multiple-effect falling film evaporator | |
| CN206631225U (en) | A kind of film-rising evaporator | |
| CN208660388U (en) | A kind of oral solution dual-effect concentrator of high production capacity | |
| CN105650929B (en) | Two-period form fume hot-water type lithium bromide absorption refrigerating set with flue gas heat-exchange unit | |
| CN207845201U (en) | A kind of cycle tubulation atmospheric evaporator | |
| CN213178894U (en) | Flue gas drive waste heat recovery heat pump system | |
| CN106512459A (en) | Concentrator based on vapor thermal gain technology | |
| CN107869860A (en) | A kind of first-class absorption type heat pump of solar energy auxiliary heating | |
| CN209333224U (en) | Aluminium polychloride production evaporation and concentration spray drying system | |
| CN109282272B (en) | Superheated steam heat drying system and method based on absorption heat pump | |
| CN205627127U (en) | MVR triple -effect evaporator | |
| CN207585143U (en) | A kind of first-class absorption type heat pump of solar energy auxiliary heating | |
| CN206252859U (en) | A kind of concentrator based on steam heating power gain techniques | |
| CN206444217U (en) | A kind of methanol rectifying system | |
| CN209221520U (en) | A kind of evaporation equipment for Calcium Chloride Production | |
| CN209425691U (en) | Hot pressing wood grain fiber cement board vapour system | |
| CN201426984Y (en) | Device for condensing sweet water by four-effect evaporator | |
| CN204910802U (en) | Self -circulation MVR heat pump evaporation system | |
| CN104324512B (en) | Thermo-compression evaporation unit | |
| CN207153134U (en) | A kind of falling film evaporation tower | |
| CN208349610U (en) | A kind of solar thermal collector low-temperature water heating circulation preparation system and water source heat pump system |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| PP01 | Preservation of patent right | ||
| PP01 | Preservation of patent right |
Effective date of registration: 20230423 Granted publication date: 20190329 |