CN207276237U - A kind of high energy-saving type thermocompression distiller - Google Patents
A kind of high energy-saving type thermocompression distiller Download PDFInfo
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- CN207276237U CN207276237U CN201721273328.6U CN201721273328U CN207276237U CN 207276237 U CN207276237 U CN 207276237U CN 201721273328 U CN201721273328 U CN 201721273328U CN 207276237 U CN207276237 U CN 207276237U
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- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 311
- 239000012153 distilled water Substances 0.000 claims abstract description 102
- 239000002994 raw material Substances 0.000 claims abstract description 84
- 238000010438 heat treatment Methods 0.000 claims abstract description 34
- 238000011084 recovery Methods 0.000 claims abstract description 27
- 238000000034 method Methods 0.000 claims abstract description 12
- 238000003825 pressing Methods 0.000 claims abstract description 12
- JEGUKCSWCFPDGT-UHFFFAOYSA-N h2o hydrate Chemical compound O.O JEGUKCSWCFPDGT-UHFFFAOYSA-N 0.000 claims abstract description 10
- 238000001704 evaporation Methods 0.000 claims description 47
- 230000008020 evaporation Effects 0.000 claims description 46
- 238000009833 condensation Methods 0.000 claims description 15
- 230000005494 condensation Effects 0.000 claims description 15
- 230000001105 regulatory effect Effects 0.000 claims description 13
- 238000004821 distillation Methods 0.000 claims description 12
- 238000000926 separation method Methods 0.000 claims description 7
- 238000000605 extraction Methods 0.000 claims description 4
- 238000010025 steaming Methods 0.000 claims description 4
- 239000012141 concentrate Substances 0.000 claims description 3
- 230000006835 compression Effects 0.000 description 7
- 238000007906 compression Methods 0.000 description 7
- 238000004064 recycling Methods 0.000 description 6
- 238000007731 hot pressing Methods 0.000 description 4
- 238000004519 manufacturing process Methods 0.000 description 4
- 229920006395 saturated elastomer Polymers 0.000 description 4
- 238000009834 vaporization Methods 0.000 description 4
- 230000008016 vaporization Effects 0.000 description 4
- 238000010521 absorption reaction Methods 0.000 description 3
- 239000012530 fluid Substances 0.000 description 3
- 230000001276 controlling effect Effects 0.000 description 2
- 238000001816 cooling Methods 0.000 description 2
- 230000007423 decrease Effects 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 239000007788 liquid Substances 0.000 description 2
- 239000007921 spray Substances 0.000 description 2
- 241000372132 Hydrometridae Species 0.000 description 1
- 238000004140 cleaning Methods 0.000 description 1
- 230000001112 coagulating effect Effects 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 239000011552 falling film Substances 0.000 description 1
- 239000010408 film Substances 0.000 description 1
- 239000006260 foam Substances 0.000 description 1
- 230000002209 hydrophobic effect Effects 0.000 description 1
- 230000008676 import Effects 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 239000003595 mist Substances 0.000 description 1
- 230000000704 physical effect Effects 0.000 description 1
- 230000005855 radiation Effects 0.000 description 1
- 239000013589 supplement Substances 0.000 description 1
- 230000000153 supplemental effect Effects 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
- 239000003643 water by type Substances 0.000 description 1
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- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
- Heat Treatment Of Water, Waste Water Or Sewage (AREA)
Abstract
High energy-saving type thermocompression distiller disclosed in the utility model, it is related to pharmacy technical field of auxiliary equipment, including heat pressing type distilled water process units 1, the heat pressing type distilled water process units 1 includes raw water water inlet system, vapo(u)rization system, raw material water heating system, distilled water humidity control system and fixed gas piece-rate system；Working steam condensate heat reclaim unit 19 is further included；The working steam condensate heat reclaim unit 19 includes working steam condensate heat level-one recover 25 and working steam condensate heat secondary recovery device 22；There is energy-saving efficiency higher, be " energy-saving and emission-reduction " innovative product, be adapted to the departments such as pharmaceutical factory, food and drink factory, hospital and biochemical scientific research to be used to prepare distilled water.
Description
Technical field
Pharmacy technical field of auxiliary equipment is the utility model is related to, particularly a kind of high energy-saving type thermocompression distiller.
Background technology
At present, the thermocompression distiller produced both at home and abroad has two kinds, and one kind is vertical type evaporator type, and another kind is horizontal
Evaporator type, its operation principle are all to employ vapour compression machine (also referred to as hot press), convert electric energy to thermal energy and are evaporated
Operation, only feed water is heated using working steam.Although energy-saving effect is in the special equipment of current production distilled water
Best, still, still suffer from problems with：
First, containing substantial amounts of heat in the condensate that working steam produces, do not recycled effectively, but in vain
White throws away, and the heat wasted can be seen that by following explanation：
By taking the thermocompression distiller of 10 tons of production capacity as an example, 10,000kg distilled water is produced per hour, must be consumed
1200kg working steams, that is, produce 1200kg condensed waters, and after testing, the discharge temperature of condensed water is 120-125 DEG C.
Condensate temperature takes t1=120 DEG C, the charging coolant-temperature gage of distillation machine is under normal circumstances 15-25 DEG C, takes centre
Value T1=20 DEG C.If with charging water cooling condensed water, then, by charging coolant-temperature gage T135 can be down to by condensate temperature by knowing
Below DEG C, 35 DEG C are taken.Specific heat at constant pressure according to water is approximately cp=1kcal/ (kg DEG C), it is known that condensed water is obtained by feed water
The heat taken is Q=1200 × cp×(t1- 35)=102000kcal.During according to thermocompression distiller normal operation, charging
The working steam meter pressure 2kgf/cm of water heater2, look into saturated vapor physical property table and obtain, the latent heat of vaporization of working steam is r=
518.1kcal/kg, working steam amount is converted into by heat Q
W=Q/r=196.9kg.
That is, often produce 10 tons of distilled water just in vain thrown away working steam 196.9kg.
If recycle these working steams, then, energy-saving efficiency can improve (196.9/1200) × 100%=
16.4%.
Second, heat recovery is more difficult：Although as you know there is larger thermal losses, to carry out above-mentioned
There are more difficulty, its main cause to be for the recycling of heat：
Above-mentioned heat can be effectively recycled to be truly realized, must just solve to produce after working steam condenses does not coagulate
The discharge problem of gas, otherwise (it is small that the distillation machine for having many pharmacy corporations runs 16 daily during heater long time continuous working
When more than, or even it is also daily 24 it is small when run), will roll up in the indoor fixed gas of working steam heating operation,
It will also be thickeied in the fixed gas film layer that heat transfer interface is formed, the thermal resistance of working steam and heat transfer interface is increased, heated
The heat transfer coefficient of device also will drastically decline, and cause the production capacity of complete machine drastically to decline or even can not normal operation.
When working steam condensate heat does not recycle, because condensate discharge pipe is shorter and it is usually from top to bottom or horizontal to be
Flowing directly under throw away in well and (therefore lower well mouth substantial amounts of steam of emerging can be frequently seen in pharmacy corporation and is showed
As), therefore will not produce effective water seal phenomenon during condensate flowing, i.e. pipeline is not sealed completely by condensate, is just had in pipeline
A small amount of vapour (gas) body flowing space, fixed gas can be emitted with vapour (gas) the body flowing space.
When the heat of working steam condensate is recycled, condensate carries out heat again after needing to be collected into heat exchanger
Recycling, i.e. condensate enter working steam condensate heat by the pipeline between heater and heat recoverer (being exactly heat exchanger) and return
Receive device, condensate line length and also tedge section, after especially condensate enters heat recoverer, because heat recoverer only uses
, could most effective carry out heat recovery during reverse-flow horizontal tubular heat exchanger.Condensate (is required according to GMP, managed in shell fluid flow
Journey is compared with shell side sanitary cleaning therefore walks raw water), shell side is equipped with baffle plate, when lateral flow of the condensate full of shell side generation heat exchanger tube
When and under the process conditions of countercurrent heat-transfer, could have best heat exchange efficiency.Otherwise, because " water → water " heat transfer effect compared with
Difference, does not just reach the maximum recycling purpose of heat in condensate at all.In this case, condensate will necessarily produce in flow process
Raw effective water seal, makes fixed gas not have passable gas passage and cannot discharge.Above reason may be exactly, both domestic and external
Thermocompression distiller can not accomplish the heat recovery of working steam condensate also so far.
Third, the work efficiency of hot press reduces：Due to the structure of traditional demister (steam-water separator), cause to steam
The pure steam venthole for sending out device is too high (at the top of evaporator) so that the pure steam outlet of evaporator and the pure steam of hot press
Connecting line between entrance it is too long (be 4m or so, the hot pressing distillation machine of especially horizontal-type evaporator is longer, about 5m with
On).Pure steam in normal work in evaporator is to be drawn into hot press pressurizeed, heated up by hot press, Zhi Houzai
Evaporation tube group shell side is sent into by hot press operation is evaporated to the raw water in tube side.Because pure steam enters the pipeline of hot press
It is long, so pure steam flow resistance increases, the inhalation power of hot press is also increased therewith, the work done during compression of hot press but subtracts therewith
It is small, cause the power consumption of the hot press under specified production capacity to increase, i.e. waste of energy.
Disclosed in Chinese patent (number of patent application 99234696.7) " thermocompression distiller ", it is by electrical equipment control
Cabinet, vapour compression machine, evaporative condenser and heat exchanger are formed, the suction inlet of vapour compression machine and the foam removal on evaporative condenser top
Room communicates, and gas outlet is connected with the vaporization chamber pipeline in the middle part of evaporative condenser, exchanger base and inlet pipeline delivery pump phase
Even, its middle part adjusts tank with outlet pipeline delivery pump and effluent recycling and is connected.
" horizontal tube falling film heat pressing type distilled water disclosed in another Chinese patent (number of patent application 201410596563.1)
Machine ", is filled by raw material water pump, heat exchanger, vaporization chamber, supplemental heater, transverse tube heater, vapour compression machine, circulating pump, spray
Put, on-condensible gas heat exchanger and distillation water collecting tank form.Raw water enters vaporization chamber after heat exchanger preheats, and adds through supplement
Hot device heating produces indirect steam, and indirect steam is formed high temperature indirect steam after vapour compression machine suction compression and added into transverse tube
In the pipe of hot device, while raw water is pumped into spray equipment by circulation, and raw water is equably sprayed outside transverse tube heater
Wall, is conducted heat by tube wall, is made the raw material water evaporation outside pipe, is successively produced indirect steam.High temperature indirect steam quilt in pipe
Condensation, produces distilled water.
Also " thermocompression distiller system " disclosed in Chinese patent (number of patent application 201520513986.2), bag
Include：Raw water heating system, horizontal-type evaporator, compressor, de- vapour tank and PLC control system, PLC control system control the raw water
Heating system, horizontal-type evaporator, compressor and the work of de- vapour tank.
The content of the invention
In view of the deficienciess of the prior art, technical problem to be solved in the utility model is to provide one kind with energy saving
More efficient thermocompression distiller.
To achieve the above object, technical solution adopted in the utility model is a kind of high energy-saving type heat pressing type distillation of design
Water dispenser, including heat pressing type distilled water process units 1, the heat pressing type distilled water process units 1 include raw water water inlet system, steam
Hair system, raw material water heating system, distilled water humidity control system and fixed gas piece-rate system；Working steam condensate is further included
Heat reclaim unit 19；
The working steam condensate heat reclaim unit 19 includes working steam condensate heat level-one recover 25 and work
Make steam condensation water heat secondary recovery device 22；
The input end of the shell side of working steam condensate heat level-one recover 25 connects raw water heating by pipeline respectively
On the one hand system and vapo(u)rization system, its port of export draw fixed gas discharge pipe 27, on the other hand by condensate connecting line 24
Connect the input end of the shell side of working steam condensate heat secondary recovery device 22；
The port of export of the tube side of working steam condensate heat level-one recover 25 connects raw material water heating system and steaming respectively
Distilled water humidity control system, its input end connect working steam condensate heat secondary recovery device 22 by pipe line at the beginning of raw water 23
Tube side the port of export, the input end of the tube side of working steam condensate heat secondary recovery device 22 passes through pipeline 20 and connects raw water
Water inlet system；
The port of export of the shell side of working steam condensate heat secondary recovery device 22 draws condensate discharge line 21.
The raw water water inlet system includes raw material water pump 13, raw material water lines 14 and condensed water heat recoverer 18,
One end connection raw material water pump 13 of raw material water lines 14, the input end of the tube side of other end connection condensed water heat recoverer 18；
The port of export of the tube side of condensed water heat recoverer 18 connects working steam condensate heat secondary recovery device 22 by pipeline 20
The input end of tube side；Concentrate one end connection vapo(u)rization system of water lines 12, the shell of other end connection condensed water heat recoverer 18
The input end of journey；Condensed water discharge line 17 is drawn by the port of export of the shell side of condensed water heat recoverer 18；
The raw material water heating system includes raw material water heater 36, and the input end of the shell side of raw material water heater 36 connects
Connect raw water heating work steam supply regulating valve and its pipeline 34；Raw water heating work steam condensation water discharge steam trap and its
The port of export of the shell side of one end connection raw material water heater 36 of pipeline 32, other end connection working steam condensate heat level-one are returned
Receive the input end of the shell side of device 25；The input end of the tube side of raw material water heater 36 on the one hand connection pneumatic control valve 29, another
Aspect connects distilled water humidity control system by temperature adjustment raw material water lines 38, and the port of export of the tube side of raw material water heater 36 leads to
Cross heating raw material water lines 37 and connect fixed gas piece-rate system；
The distilled water humidity control system includes distilled water thermoregulator 39, distilled water surge tank 9 and distilled water
Pump 15；The input end of the shell side of distilled water thermoregulator 39 makees steam condensation water heat level-one recover 25 by the connection of pipeline 28
Tube side the port of export, the port of export of the shell side of distilled water thermoregulator 39 passes through temperature adjustment raw material water lines 38 and connects raw water
The input end of the tube side of heater 36；The input end of the tube side of distilled water thermoregulator 39 by distilled water intermediate duct 16 according to
Secondary connection distilled water pump 15, distillation water lines 11, distilled water surge tank 9 and vapo(u)rization system, the pipe of distilled water thermoregulator 39
The port of export of journey discharges distilled water by distilled water discharge line 35；Fixed gas draws the one of pipeline 42 in distilled water and pure steam
End connection distilled water surge tank 9, other end connection fixed gas piece-rate system；
The fixed gas piece-rate system includes fixed gas separator 40, and one end connection of heating raw material water lines 37 is not coagulated
The entrance of gas separating device 40, the port of export of the tube side of other end connection raw material water heater 36；Fixed gas discharge line 41 is not by
Solidifying gas separating device 40 is drawn, and the both ends of fixed gas extraction pipeline 42 connect distilled water surge tank 9 respectively in distilled water and pure steam
With fixed gas separator 40, the both ends of separation raw material water lines 10 connect outlet and the evaporation system of fixed gas separator 40 respectively
System；
The vapo(u)rization system includes evaporator 43, hot press 4, evaporation tube group 6, startup evaporation tube group 8 and condensed water limit
Position discharge pipe 7, evaporation tube group 6 and startup evaporation tube group 8 are separately mounted to the middle and lower part and lower part of 43 inner cavity of evaporator, condensed water
Spacing discharge pipe 7 is installed on the centre of 43 inner cavity lower part of evaporator and connects condensed water heat recovery by concentrating water lines 12
The input end of the shell side of device 18；Hot press 4 connects evaporator 43 by pure steam entrance pipe 3, and passes through pure steam outlet
Road 5 connects evaporation tube group 6；The shell side of evaporation tube group 6 is also connected with distilled water surge tank 9；Separate the both ends of raw material water lines 10
The outlet of fixed gas separator 40 and the lower lumen of evaporator 43 are connected respectively；The working steam that hot press starts evaporator supplies
Start the input end of evaporation tube group 8 to regulating valve and its connection of pipeline 31, start the port of export of evaporation tube group 8 by starting work
Steam condensation water discharge line 30 connects the input end of the shell side of working steam condensate heat level-one recover 25.
On the inner cavity top of the evaporator 43, demister (also referred to as steam-water separator) 2, the pure steam are additionally provided with
Entrance pipe 3 is by the inner cavity middle and upper part through evaporator 43 is drawn and is connected with hot press 4 downwards among the top of demister 2.
The evaporation tube group 6 is vertical tube evaporation tube group.
The startup evaporation tube group 8 is c-type evaporation tube group.
Throttle orifice 33 is additionally provided with the port of export of the shell side of the raw material water heater 36, and passes through fixed gas fairlead
Road 26 connects the input end of the shell side of working steam condensate heat level-one recover 25.
The high energy-saving type thermocompression distiller of the utility model：
First, employing the working steam condensate heat reclaim unit of two-stage countercurrent heat-exchanging process flow, i.e., condensate is by high temperature
Section is flowed to low-temperature zone, and raw water is flowed from low-temperature zone to high temperature section, therefore, is increased effective heat transfer temperature difference, is improved heat exchange
Efficiency, enables raw water to absorb the heat in condensate to greatest extent, brings into machine and be used again.With the current country
Outer thermocompression distiller is compared, its energy-saving efficiency improves more than 15%.
Second, by the outlet of pure steam entrance pipe positioned at the lower section of demister, and heat pressing type distilled water both domestic and external at present
The pure steam of machine is exported all at the top of the evaporator of the top of demister.Due to the outlet position of the pure steam entrance pipe of demister
Put relatively low, enter vapour close to hot press (current hot press be actually sleeping ox formula high-temperature centrifugal fan, axial air intake)
Mouthful so that the length of connecting tube it is very short [be only 0.6m, for the pipe range of other domestic hot pressing distillation machines (0.6 ÷ 4) ×
100%=15%], therefore, the resistance and radiation loss energy of pure steam flowing greatly reduces, while also reduce hot pressing
The suction work(of machine, saves power consumption, improves the work efficiency of hot press.
Brief description of the drawings
Fig. 1 is the principle schematic diagram of the utility model.
In figure：
1 is heat pressing type distilled water process units, and 2 be demister, and 3 be pure steam entrance pipe, and 4 be hot press, and 5 be pure steaming
Vapor outlet pipeline, 6 be evaporation tube group, and 7 be the spacing discharge pipe of condensed water, and 8 be to start evaporation tube group, and 9 be distilled water surge tank, 10
It is separation raw material water lines, 11 be distillation water lines, and 12 be concentration water lines, and 13 be raw material water pump, and 14 be raw material water lines, 15
It is distilled water pump, 16 be distilled water intermediate duct, and 17 be condensed water discharge line, and 18 be condensed water heat recoverer, and 19 be work
Make steam condensation water heat reclaim unit, 20 be pipeline, and 21 be condensate discharge line, and 22 be working steam condensate heat secondary recovery
Device, 23 be raw water just pipe line, and 24 be condensate connecting line, and 25 be working steam condensate heat level-one recover, and 26 be not
Solidifying gas draws pipeline, and 27 be fixed gas discharge pipe, and 28 be pipeline, and 29 be pneumatic control valve, and 30 be the discharge of working steam condensate
Steam trap and its pipeline, 31 be the working steam supply regulating valve and its pipeline that hot press starts evaporator, and 32 be that raw water adds
Thermal technology makees steam condensation water discharge steam trap and its pipeline, and 33 be throttle orifice, and 34 be raw water heating work steam supply regulating valve
And its pipeline, 35 be distilled water discharge line, and 36 be raw material water heater, and 37 be heating raw material water lines, and 38 be temperature adjustment raw material
Water lines, 39 be distilled water thermoregulator, and 40 be fixed gas separator, and 41 be fixed gas discharge line, 42 be distilled water and
Fixed gas draws pipeline in pure steam, and 43 be evaporator.
Embodiment
Below in conjunction with drawings and examples, the utility model is further described.Following explanation is to use to enumerate
Mode, but the scope of protection of the utility model should not be limited to thoses mentioned above.
The present embodiment is the vertical hot pressing distillation machine of high energy-saving type, is by vertical heat pressing type distilled water process units 1, work
Make steam condensation water heat reclaim unit 19 to form.
Vertical heat pressing type distilled water process units 1 be by raw water water inlet system, vapo(u)rization system, raw material water heating system,
Distilled water humidity control system and fixed gas piece-rate system are formed；Working steam condensate heat reclaim unit 19 is by working steam
Condensate heat level-one recover 25 and working steam condensate heat secondary recovery device 22 are formed.
Working steam condensate heat level-one recover 25 employs vertical tube-type heat exchanger, and there are vapour-liquid two at the same time for shell side
Phase fluid space so that vapour (gas), liquid have sufficient heat transfer space, the shell side of working steam condensate heat level-one recover 25
Input end connects raw material water heating system and vapo(u)rization system by pipeline respectively, on the one hand its port of export draws fixed gas delivery pipe
Road 27, on the other hand connected by condensate connecting line 24 working steam condensate heat secondary recovery device 22 shell side import
End.
The port of export of the tube side of working steam condensate heat level-one recover 25 connects raw material water heating system and steaming respectively
Distilled water humidity control system, its input end connect working steam condensate heat secondary recovery device 22 by pipe line at the beginning of raw water 23
Tube side the port of export, the input end of the tube side of working steam condensate heat secondary recovery device 22 passes through pipeline 20 and connects raw water
Water inlet system.
The port of export of the shell side of working steam condensate heat secondary recovery device 22 draws condensate discharge line 21.
Raw water water inlet system includes raw material water pump 13, raw material water lines 14 and condensed water heat recoverer 18, raw water
One end connection raw material water pump 13 of pipeline 14, the input end of the tube side of other end connection condensed water heat recoverer 18；Condensed water
The port of export of the tube side of heat recoverer 18 connects the tube side of working steam condensate heat secondary recovery device 22 by pipeline 20
Input end；Concentrate one end connection vapo(u)rization system of water lines 12, the shell side of other end connection condensed water heat recoverer 18 into
Mouth end；Condensed water discharge line 17 is drawn by the port of export of the shell side of condensed water heat recoverer 18.
Raw material water heating system includes raw material water heater 36, the input end connection raw material of the shell side of raw material water heater 36
Water heating work steam supplies regulating valve and its pipeline 34；Raw water heating work steam condensation water discharges steam trap and its pipeline 32
One end connection raw material water heater 36 shell side the port of export, other end connection working steam condensate heat level-one recover 25
Shell side input end；On the one hand the input end of the tube side of raw material water heater 36 connects pneumatic control valve 29, on the other hand leads to
Cross temperature adjustment raw water pipeline 38 and connect distilled water humidity control system, the port of export of the tube side of raw material water heater 36 passes through heating
Raw material water lines 37 connect fixed gas piece-rate system；Throttling is additionally provided with the port of export of the shell side of the raw material water heater 36
Hole 33, and the input end of the shell side by the fixed gas extraction connection working steam condensate heat level-one of pipeline 26 recover 25.
Distilled water humidity control system includes distilled water thermoregulator 39, distilled water surge tank 9 and distilled water pump 15；Steam
The input end of the shell side of distilled water thermoregulator 39 connects the tube side for making steam condensation water heat level-one recover 25 by pipeline 28
The port of export, the port of export of the shell side of distilled water thermoregulator 39 passes through temperature adjustment raw material water lines 38 and connects raw material water heater
The input end of 36 tube side；The input end of the tube side of distilled water thermoregulator 39 is sequentially connected by distilled water intermediate duct 16
Distilled water pump 15, distillation water lines 11, distilled water surge tank 9 and vapo(u)rization system, the tube side of distilled water thermoregulator 39 go out
Mouth end passes through distilled water discharge line 35 and discharges distilled water；One end that distilled water draws pipeline 42 with fixed gas in pure steam connects
Distilled water surge tank 9, other end connection fixed gas piece-rate system.
Fixed gas piece-rate system includes fixed gas separator 40, one end connection fixed gas separation of heating raw material water lines 37
The entrance of device 40, the port of export of the tube side of other end connection raw material water heater 36；Fixed gas discharge line 41 is by fixed gas point
Drawn from device 40, the both ends of fixed gas extraction pipeline 42 connect distilled water surge tank 9 and do not coagulate respectively in distilled water and pure steam
Gas separating device 40, the both ends of separation raw material water lines 10 connect outlet and the vapo(u)rization system of fixed gas separator 40 respectively.
Vapo(u)rization system includes evaporator 43, hot press 4, evaporation tube group 6, startup evaporation tube group 8 and the spacing discharge of condensed water
Pipe 7, evaporation tube group 6 (for vertical tube evaporation tube group) and startup evaporation tube group 8 are separately mounted to evaporate (for c-type evaporation tube group)
The middle and lower part and lower part of 43 inner cavity of device, the spacing discharge pipe 7 of condensed water are installed on the centre of 43 inner cavity lower part of evaporator and by dense
Shrink pipeline 12 connects the input end of the shell side of condensed water heat recoverer 18；Hot press 4 is connected by pure steam entrance pipe 3
Evaporator 43, and evaporation tube group 6 is connected by pure steam export pipeline 5；Evaporation tube group 6 is also connected with distilled water surge tank 9；Point
Both ends from raw material water lines 10 connect the outlet of fixed gas separator 40 and the lower lumen of evaporator 43 respectively；Hot press opens
The working steam supply regulating valve of dynamic evaporator and its connection of pipeline 31 start one end of evaporation tube group 8, start evaporation tube group 8
The other end discharges steam trap by working steam condensate and its pipeline 30 connects working steam condensate heat level-one recover 25
The input end of shell side.
On the inner cavity top of the evaporator 43, demister 2 is additionally provided with, the pure steam entrance pipe 3 is by demisting
The inner cavity middle and upper part through evaporator 43 is drawn and is connected with hot press 4 downwards among the top of device 2.
During use：Raw water is sequentially sent into raw material water lines 14, the pipe of condensed water heat recoverer 18 by raw material water pump 13
Just pipe line 23, working steam condensate are hot for journey, pipeline 20, the tube side of working steam condensate heat secondary recovery device 22, raw water
Measure tube side, pipeline 28, pneumatic control valve 29 and its shell of place pipeline and distilled water thermoregulator 39 of level-one recover 25
(temperature adjustment raw material water lines 38 and pneumatic control valve 29 and its place pipeline are to be connected in parallel, big portion for journey, temperature adjustment raw material water lines 38
Raw water is divided to flow into raw material water heater 36 through distilled water thermoregulator 39, temperature adjustment raw material water lines 38 by pipeline 28, few portion
Point raw water flows into raw material water heater 36 through pneumatic control valve 29 and its place pipeline), heating raw material water lines 37, fixed gas
Separator 40, separation raw material water lines 10 flow into the inner cavity lower part of evaporator 43.Raw water, flows into condensed water heat recoverer 18
Tube side when will flow through its shell side condensed water heat absorption, flow into the tube side of working steam condensate heat secondary recovery device 22
When by the heat absorption of the condensate in its shell side, by its shell side when flowing into the tube side of working steam condensate heat level-one recover 25
In condensate, water vapour, the heat absorption of fixed gas, by the working steam of its shell side when flowing into the tube side of raw material water heater 36
Heating, by fixed gas after the fixed gas in its own is separated in the state of raw water sprinkling when flowing into fixed gas separator 40
Discharge line 41 discharges, and flows into evaporator 43 afterwards and is evaporated into water vapour.The raw water not being evaporated becomes condensed water, by
The concentrated water lines 12 of the spacing discharge pipe of condensed water, which are flowed into the shell side of condensed water heat recoverer 18, is transmitted to the heat of itself
Raw water, the concentrated discharge of water discharge pipe road 17 afterwards is thrown away or recycling.Start shooting the starting stage, raw water is activated
Evaporation tube group 8 is evaporated, and the water vapour of generation is wet saturated vapor, and wet saturated vapor rises through (the efficient silk screen of demister 2
Demister) except pure steam (i.e. dry saturated vapor) is become after the mist in devaporation, pure steam is inhaled through pure steam entrance pipe 3
Enter and pressurization heating carried out in hot press 4, after through pure steam export pipeline 5 flow into the shell side of evaporation tube group 6 to the original in tube side
Material water is evaporated, and itself is condensed into distilled water.When hot press 4 independently can be evaporated operation, start evaporation tube
Group 8 will stop evaporating work, i.e., hot press starts the working steam supply regulating valve of evaporator and its pipeline 31 is closed and stopped
Working steam supplies.
Distilled water and fixed gas flow into distilled water surge tank by the shell side of the vertical row standard vertical tube evaporator group 6 in evaporator 43
9, fixed gas is drawn pipeline 42 through fixed gas in distilled water and pure steam and is flowed into fixed gas separator 40, wherein what is leaked is few
The raw water that the pure steam of amount is sprayed is condensed into condensate and is blended in raw water, and fixed gas is discharged by fixed gas discharge line 41
Go out.
Distilled water in distilled water surge tank 9 is sequentially sent into distilled water intermediate tube through distilling water lines 11 by distilled water pump 15
Road 16, the tube side of distilled water thermoregulator 39, distilled water discharge line 35, flow out machine by distilled water discharge line 35.Steam
A part of heat is transmitted to raw water itself after the tube side of distilled water inflow distilled water thermoregulator 39 and is cooled to controlling value 82-86
DEG C, controlling value is by adjusting flow of (cold fluid) feed water stream through distilled water thermoregulator 39 by pneumatic control valve 29
(changing cooling load) is come what is realized.
Working steam in the working steam supply regulating valve and its pipeline 31 of hot press startup evaporator, steams into starting
Hair pipe group 8 is evaporated the raw water in evaporator 43, and it is hydrophobic by the discharge of working steam condensate itself to be condensed into condensate
Device and its pipeline 30 (including steam trap) flow into the shell side of working steam condensate heat level-one recover 25, when 4 energy of hot press
Enough it is normally carried out that hot press after evaporation operation starts the working steam supply regulating valve of evaporator and its pipeline 31 closes and stops supplying
Vapour, that is, start evaporation tube group 8 and stop evaporation work；Raw water heating work steam supplies the work in regulating valve and its pipeline 34
Steam, the shell side into raw material water heater 36 heats raw water, and itself is condensed into condensate and is heated by raw water
Working steam condensate discharges steam trap and its pipeline 32 (including steam trap) flows into working steam condensate heat level-one recover
25 shell side.The fixed gas produced in the shell side of raw material water heater 36 after working steam condensation is drawn by throttle orifice 33 through fixed gas
Go out the shell side that pipeline 26 flows into working steam condensate heat level-one recover 25, draw and leak minimal amount of with fixed gas
Working steam is flowed into other condensates by raw material water condensation in tube side into condensate, and fixed gas is discharged by fixed gas discharge pipe 27.
After heat is transmitted to the raw water in its tube side by the condensate in 25 shell side of working steam condensate heat level-one recover, connected by condensate
Heat is again passed to raw water in the shell side of adapter road 24 inflow working steam condensate heat secondary recovery device 22, afterwards by coagulating
The discharge of water discharge pipe road 21 is thrown away or recycling.
The high energy-saving type thermocompression distiller of the utility model, is adapted to pharmaceutical factory, food and drink factory, hospital and biochemical section
Yan Deng departments are used to prepare distilled water.
Claims (6)
1. a kind of high energy-saving type thermocompression distiller, including heat pressing type distilled water process units (1), the heat pressing type distilled water
Process units (1) includes raw water water inlet system, vapo(u)rization system, raw material water heating system, distilled water humidity control system and not
Solidifying gas separating system；It is characterized in that：Working steam condensate heat reclaim unit (19) is further included；
The working steam condensate heat reclaim unit (19) includes working steam condensate heat level-one recover (25) and work
Make steam condensation water heat secondary recovery device (22)；
The input end of the shell side of working steam condensate heat level-one recover (25) connects raw water heating system by pipeline respectively
On the one hand system and vapo(u)rization system, its port of export draw fixed gas discharge pipe (27), on the other hand by condensate connecting line
(24) input end of the shell side of working steam condensate heat secondary recovery device (22) is connected；
The port of export of the tube side of working steam condensate heat level-one recover (25) connects raw material water heating system and distillation respectively
Coolant-temperature gage regulating system, its input end connect working steam condensate heat secondary recovery device by pipe line at the beginning of raw water (23)
(22) port of export of tube side, the input end of the tube side of working steam condensate heat secondary recovery device (22) are connected by pipeline (20)
Connect raw water water inlet system；
The port of export of the shell side of working steam condensate heat secondary recovery device (22) draws condensate discharge line (21).
2. high energy-saving type thermocompression distiller according to claim 1, it is characterised in that：
The raw water water inlet system includes raw material water pump (13), raw material water lines (14) and condensed water heat recoverer
(18), one end connection raw material water pump (13) of raw material water lines (14), the pipe of other end connection condensed water heat recoverer (18)
The input end of journey；The port of export of the tube side of condensed water heat recoverer (18) connects working steam condensate heat by pipeline (20)
The input end of the tube side of secondary recovery device (22)；Concentrate one end connection vapo(u)rization system of water lines (12), other end connection concentration
The input end of the shell side of water heat recoverer (18)；Condensed water discharge line (17) by condensed water heat recoverer (18) shell side
The port of export draw；
The raw material water heating system includes raw material water heater (36), and the input end of the shell side of raw material water heater (36) connects
Connect raw water heating work steam supply regulating valve and its pipeline (34)；Raw water heating work steam condensation water discharge steam trap and
The port of export, the other end connection working steam condensate heat of the shell side of one end connection raw material water heater (36) of its pipeline (32)
The input end of the shell side of level-one recover (25)；The input end of the tube side of raw material water heater (36) on the one hand connects pneumatic adjust
Valve (29), on the other hand connect distilled water humidity control system, raw material water heater (36) by temperature adjustment raw material water lines (38)
Tube side the port of export by heat raw material water lines (37) connect fixed gas piece-rate system；
The distilled water humidity control system includes distilled water thermoregulator (39), distilled water surge tank (9) and distilled water
Pump (15)；The input end of the shell side of distilled water thermoregulator (39) is made steam condensation water heat level-one by pipeline (28) connection and is returned
The port of export of the tube side of device (25) is received, the port of export of the shell side of distilled water thermoregulator (39) passes through temperature adjustment raw material water lines
(38) input end of the tube side of raw material water heater (36) is connected；The input end of the tube side of distilled water thermoregulator (39) passes through
Distilled water intermediate duct (16) is sequentially connected distilled water pump (15), distillation water lines (11), distilled water surge tank (9) and evaporation system
System, the port of export of the tube side of distilled water thermoregulator (39) discharge distilled water by distilled water discharge line (35)；Distilled water
One end that pipeline (42) is drawn with fixed gas in pure steam connects distilled water surge tank (9), other end connection fixed gas segregative line
System；
The fixed gas piece-rate system includes fixed gas separator (40), and one end connection of heating raw material water lines (37) is not coagulated
The entrance of gas separating device (40), the port of export of the tube side of other end connection raw material water heater (36)；Fixed gas discharge line
(41) drawn by fixed gas separator (40), the both ends of fixed gas extraction pipeline (42) connect steaming respectively in distilled water and pure steam
Distilled water surge tank (9) and fixed gas separator (40), the both ends of separation raw material water lines (10) connect fixed gas separator respectively
(40) outlet and vapo(u)rization system；
The vapo(u)rization system includes evaporator (43), hot press (4), evaporation tube group (6), startup evaporation tube group (8) and concentration
The spacing discharge pipe of water (7), evaporation tube group (6) and startup evaporation tube group (8) are separately mounted to the middle and lower part of evaporator (43) inner cavity
And lower part, the spacing discharge pipe of condensed water (7) are installed on the centre of evaporator (43) inner cavity lower part and by concentrating water lines (12)
Connect the input end of the shell side of condensed water heat recoverer (18)；Hot press (4) is connected by pure steam entrance pipe (3) to be evaporated
Device (43), and evaporation tube group (6) is connected by pure steam export pipeline (5)；The shell side of evaporation tube group (6) is also buffered with distilled water
Tank (9) connects；The both ends of separation raw material water lines (10) connect outlet and the evaporator (43) of fixed gas separator (40) respectively
Lower lumen；Start working steam supply regulating valve and its pipeline (31) connection starts the input end of evaporation tube group (8), start
The port of export of evaporation tube group (8) discharges steam trap by working steam condensate and its pipeline (30) connects working steam condensate heat
The input end of the shell side of level-one recover (25).
3. high energy-saving type thermocompression distiller according to claim 2, it is characterised in that：In the evaporator (43)
Inner cavity top, is additionally provided with demister (2), the pure steam entrance pipe (3) among the top of demister (2) by passing through downwards
Draw and be connected with hot press (4) in the inner cavity middle and upper part of evaporator (43).
4. high energy-saving type thermocompression distiller according to claim 3, it is characterised in that：The evaporation tube group (6)
For vertical tube evaporation tube group.
5. high energy-saving type thermocompression distiller according to claim 4, it is characterised in that：The startup evaporation tube group
(8) it is c-type evaporation tube group.
6. high energy-saving type thermocompression distiller according to claim 5, it is characterised in that：In the raw material water heater
(36) port of export of shell side is additionally provided with throttle orifice (33), and draws pipeline (26) by fixed gas and connect working steam condensate
The input end of the shell side of heat level-one recover (25).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721273328.6U CN207276237U (en) | 2017-09-29 | 2017-09-29 | A kind of high energy-saving type thermocompression distiller |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721273328.6U CN207276237U (en) | 2017-09-29 | 2017-09-29 | A kind of high energy-saving type thermocompression distiller |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN207276237U true CN207276237U (en) | 2018-04-27 |
Family
ID=61988584
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201721273328.6U Withdrawn - After Issue CN207276237U (en) | 2017-09-29 | 2017-09-29 | A kind of high energy-saving type thermocompression distiller |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN207276237U (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107473298A (en) * | 2017-09-29 | 2017-12-15 | 曲景春 | A kind of high energy-saving type thermocompression distiller |
| CN113175834A (en) * | 2021-05-24 | 2021-07-27 | 南京工业大学 | Pharmaceutical factory equipment waste heat utilization system and method applying separated heat pipe and phase-change material |
| WO2022187910A1 (en) * | 2021-03-11 | 2022-09-15 | Ellen Medical Devices Pty Ltd | System, method and device for treating a liquid |
-
2017
- 2017-09-29 CN CN201721273328.6U patent/CN207276237U/en not_active Withdrawn - After Issue
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107473298A (en) * | 2017-09-29 | 2017-12-15 | 曲景春 | A kind of high energy-saving type thermocompression distiller |
| CN107473298B (en) * | 2017-09-29 | 2023-04-04 | 曲景春 | High energy-saving hot-pressing distilled water machine |
| WO2022187910A1 (en) * | 2021-03-11 | 2022-09-15 | Ellen Medical Devices Pty Ltd | System, method and device for treating a liquid |
| CN113175834A (en) * | 2021-05-24 | 2021-07-27 | 南京工业大学 | Pharmaceutical factory equipment waste heat utilization system and method applying separated heat pipe and phase-change material |
| CN113175834B (en) * | 2021-05-24 | 2024-05-24 | 南京工业大学 | Pharmaceutical factory equipment waste heat utilization system and method using separated heat pipes and phase change materials |
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Effective date of registration: 20210906 Address after: 201600 floor 5, building 31, No. 2050, Dingsheng Road, Songjiang District, Shanghai Patentee after: Xinano Pharmaceutical Technology (Shanghai) Co.,Ltd. Address before: 410116 Hunan Xinzhong Pharmaceutical Machinery Co., Ltd., 109 Xinxing Road, Yuhua District, Changsha City, Hunan Province Patentee before: Qu Jingchun |
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