CN209451346U - A kind of high-efficiency condensation device - Google Patents
A kind of high-efficiency condensation device Download PDFInfo
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- CN209451346U CN209451346U CN201920067916.7U CN201920067916U CN209451346U CN 209451346 U CN209451346 U CN 209451346U CN 201920067916 U CN201920067916 U CN 201920067916U CN 209451346 U CN209451346 U CN 209451346U
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- water
- drier
- pipe
- water purifier
- condensation device
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Abstract
The utility model provides a kind of high-efficiency condensation device, including air inlet pipeline and inlet pipeline, drier and condensing tower are disposed on the air inlet pipeline, the air inlet of air inlet pipeline and the input terminal of drier connect, the output end of drier and the air intake at the top of condensing tower connect, condensing tower lower part is provided with outlet pipe, and high-temperature gas is drained into next procedure by outlet pipe；Water purifier and the condensing tower are disposed on the inlet pipeline, the water inlet of inlet pipeline and the input terminal of water purifier connect, the water inlet for the spiral cold-finger being arranged in the output end of water purifier and condensing tower is connected, and cooling water is discharged outside condensing tower the water outlet of spiral cold-finger；The condensation tower bottom is connected with collecting tank, and the drier is silica gel drier.The utility model, which provides, needs to design that a kind of drying efficiency is high, structure is simple, product purity high-efficiency condensation device.
Description
Technical field
The utility model relates to a kind of high-efficiency condensation devices, more particularly to a kind of recycling applied in waste rubber goods
The high-efficiency condensation device in production line is recycled, chemical equipment technical field is belonged to.
Background technique
Dimethyl carbonate abbreviation DMC, is a kind of industrial chemicals less toxic, environmental-protecting performance is excellent, widely used, it is a kind of
Important organic synthesis intermediate has a variety of reactivity containing functional groups such as carbonyl, methyl and methoxyl groups in molecular structure
Can, have the characteristics that in production using conveniently, safely, pollution less, be easy transport.Since dimethyl carbonate toxicity is smaller, it is
A kind of " green " chemical products with development prospect.The production line that DMC is recycled is the leftover pieces using DMC material, such as
Nipple, electrical appliance shell etc., by broken → reaction → condensation collection → neutralization reaction → adsorption bleaching → plate compression → liquid at
Product DMC.
The admission line of the condensing tower of the waste recovery technique for DMC of the prior art is usually to use single silica gel
Molecular sieve and silica dehydrator floor are either superimposed to form dehydration and drying area by desiccant, and the comparatively dense gap of dry section is less, no
Drying layer dehydration and drying is run through conducive to gas, and gas is easy the one side in contact drying area, causes uneven drying
The phenomenon that, the gas condensation not being dehydrated has brought water in product into, reduces the purity of product, increases the work of later purification
Amount.
Therefore, it is necessary to design, a kind of drying efficiency is high, structure is simple, product purity high-efficiency condensation device.
Summary of the invention
To solve the above-mentioned problems of the prior art, the utility model offer needs to design that a kind of drying efficiency is high, knot
Structure is simple, product purity high-efficiency condensation device.
The utility model provides a kind of high-efficiency condensation device, including air inlet pipeline and inlet pipeline, on the air inlet pipeline
It is disposed with drier and condensing tower, the air inlet of air inlet pipeline and the input terminal of drier connect, the output end of drier
It is connect with the air intake at the top of condensing tower, condensing tower lower part is provided with outlet pipe, and high-temperature gas is drained into Xia Dao by outlet pipe
Process；Be disposed with water purifier and the condensing tower on the inlet pipeline, the water inlet of inlet pipeline and water purifier it is defeated
Enter end connection, the water inlet for the spiral cold-finger being arranged in the output end and condensing tower of water purifier is connected, and spiral cold-finger goes out
Cooling water is discharged outside condensing tower at the mouth of a river；The condensation tower bottom is connected with collecting tank, and the drier is silica gel drier.
Silica gel drier includes main unit for dryer as a further improvement of the utility model, the main unit for dryer
Input terminal is connected with air inlet, and the output end of main unit for dryer is connected with the air intake at the top of condensing tower, main unit for dryer
It is inside provided with several layers grid, silica dehydrator layer is provided on grid, forms a cavity between grid described in adjacent two layers
Layer.
4-8 layers of grid are provided in main unit for dryer as a further improvement of the utility model,.
The height of cavity layer is 50-100mm as a further improvement of the utility model,.
Water purifier includes shell as a further improvement of the utility model, and shell one end is provided with water purifier input terminal,
The water purifier input terminal is connected with the water inlet of inlet pipeline, and the shell other end is provided with water purifier output end, described net
Hydrophone output end is connected with the water inlet of condenser pipe, and the inside of the shell is disposed with from close to water inlet to water outlet
Coarse filtration area, thin filtering area, magnetized filtering area and ion-exchange area.
Coarse filtration cavity, coarse filtration area are provided between shell and coarse filtration area as a further improvement of the utility model,
Fine filtering cavity is provided between thin filtering area.
Coarse filtration cavity bottom is connected with coarse filtration impurity by conical collecting pipe and receives as a further improvement of the utility model,
Header, fine filtering cavity bottom are connected with fine filtering impurity collecting box by conical collecting pipe.
Water purifier further includes having from scale removal mechanism as a further improvement of the utility model, described from scale removal mechanism packet
Backflushing water intake pipe and recoil outlet pipe are included, the backflushing water intake pipe is connected with shell right end, recoil outlet pipe and shell left end
It is connected.
Conical collecting pipe includes cone-shaped collection bucket and enrichment pipe, cone-shaped collection as a further improvement of the utility model,
The big end of bucket is connected with coarse filtration cavity or fine filtering cavity, and the small end of cone-shaped collection bucket connects enrichment pipe, is provided on enrichment pipe
Control valve.
Control valve is provided on backflushing water intake pipe and recoil outlet pipe as a further improvement of the utility model,.
Compared with prior art, the utility model has the beneficial effects that:
1, the high-efficiency condensation device of the utility model is provided with drier, has cavity layer between the grid among drier,
Grid is relatively thin so that resistance very little when gas is by every layer, be conducive to gas quickly through, and drier from input terminal to
The dosage of silica-gel desiccant in the grid of output end be it is incremental, after the grid close from air inlet absorbs water saturation, silicon particle
Son expansion, will not still stop passing through for gas, be conducive to making full use of for silica gel particle, energy saving.
2, the high-efficiency condensation device of the utility model can dehydrate, and improve the purity for the product that condensation is collected.
3, the high-efficiency condensation device of the utility model is provided with the water purifier of scale removal effect, and the water purifier is provided with slightly mistake
Area, thin filtering area, magnetized filtering area and ion-exchange area are filtered, coarse solid particle, the tiny solid in heat transferring medium can be removed
Particle and heavy metal ion prevent that fouling occurs in the condenser pipe of condensing unit, improve the service life of equipment, guarantee heat exchange effect
The stability of rate.
4, it is respectively set between the case of water purifier in the utility model and coarse filtration area, between coarse filtration area and thin filtering
There are coarse filtration cavity and fine filtering cavity, the advanced coarse filtration area of crossing of heat transferring medium carries out preliminary coarse filtration, and coarse solid particle is blocked
In the coarse filtration cavity of coarse filtration area side, then heat transferring medium enters thin filtering area fine filtering, tiny solid particle quilt
It is blocked on thin filtering fine filtering cavity, this set energy dispersion solid particle makes water purifier in filtering area side deposition
It is not easy to block, improves the filter efficiency of condensing unit, guarantees efficient condensation effect.
5, the water purifier in the utility model is additionally provided with from scale removal mechanism, is rinsed by reverse flow, by coarse filtration area
It washes from, peel off with the scale adhered on thin filtering area, fall into impurity collecting box, avoid replacement filtering area, reduce cost, improve behaviour
Make easy degree.
6, the utility model structure is simple, easy to operate, versatile, is suitble to industrial production to use, good market prospect.
Detailed description of the invention
Fig. 1 is the structural schematic diagram of the high-efficiency condensation device of the utility model；
Fig. 2 is the enlarged structure schematic diagram of drier；
Fig. 3 is the enlarged structure schematic diagram of water purifier.
In figure: drier 1, condensing tower 2, air inlet 3, air intake 4, outlet pipe 5, water purifier 6, water inlet 7, spiral is cold
Solidifying pipe 8, water inlet 9, water outlet 10, collecting tank 11, silica gel drier 12, main unit for dryer 13, grid 14, cavity layer 15, shell
Body 16, water purifier input terminal 17, water purifier output end 18, coarse filtration area 19, thin filtering area 20, magnetized filtering area 21, ion are handed over
Change area 22, coarse filtration cavity 23, fine filtering cavity 24, conical collecting pipe 25, coarse filtration impurity collecting box 26, fine filtering impurity collecting box 27,
Backflushing water intake pipe 28, recoil outlet pipe 29, cone-shaped collection bucket 30, enrichment pipe 31.
Specific embodiment
To facilitate the understanding of the present invention, a more comprehensive description of the invention is given in the following sections with reference to the relevant attached drawings.In attached drawing
Give better embodiment of the invention.But the invention can be realized in many different forms, however it is not limited to herein
Described embodiment.On the contrary, the purpose of providing these embodiments is that making to understand more the disclosure
Add thorough and comprehensive.
When component is referred to as " being set to " another component, it can directly on the other part or there may also be
Component placed in the middle, " setting " indicate a kind of existing mode, can be connection, install, are fixedly connected, the connection sides such as activity connection
Formula.When a component is considered as " connection " another component, it can be directly to another component or may be same
When there are components placed in the middle.Term as used herein "vertical", "horizontal", "left" and "right" and similar statement are
For illustrative purposes, it is not meant to be the only embodiment.
Unless otherwise defined, all technical and scientific terms used herein and belong to technical field of the invention
The normally understood meaning of technical staff is identical.Term as used herein in the specification of the present invention is intended merely to description tool
The purpose of the embodiment of body, it is not intended that in the limitation present invention.Term " and or " used herein includes one or more
Any and all combinations of relevant listed item.
Referring to Fig. 1-3, the utility model provides a kind of high-efficiency condensation device, including air inlet pipeline and inlet pipeline, described
Drier 1 and condensing tower 2 are disposed on air inlet pipeline, the air inlet 3 of air inlet pipeline is connect with the input terminal of drier 1,
The output end of drier 1 is connect with the air intake 4 at 2 top of condensing tower, and 2 lower part of condensing tower is provided with outlet pipe 5, outlet pipe
High-temperature gas is drained into next procedure by 5；Water purifier 6 and the condensing tower 2, inlet pipeline are disposed on the inlet pipeline
Water inlet 7 connect with the input terminal of water purifier 6, the spiral cold-finger 8 being arranged in the output end of water purifier 6 and condensing tower 2
Water inlet 9 is connected, and cooling water is discharged outside condensing tower 2 water outlet 10 of spiral cold-finger 8；2 bottom of condensing tower is connected with
Collecting tank 11, the drier 1 are silica gel drier 12.
Silica gel drier 12 includes main unit for dryer 13, the drier sheet as a further improvement of the utility model,
The input terminal of body 13 is connected with air inlet 3, and the output end of main unit for dryer 13 is connected with the air intake 4 at 2 top of condensing tower,
It is provided with several layers grid 14 in main unit for dryer 13, silica dehydrator layer, lattice described in adjacent two layers are provided on grid 14
A cavity layer 15 is formed between grid 14.The high-efficiency condensation device of the utility model is provided with drier, the grid among drier
Have cavity layer 15 between 14, grid 14 is relatively thin so that resistance very little when gas is by every layer, be conducive to gas quickly through,
And the dosage of the silica-gel desiccant in grid 14 of the drier from input terminal to output end be it is incremental, when close from air inlet
After the water suction saturation of grid 14, silica gel particle expansion will not still stop passing through for gas, be conducive to making full use of for silica gel particle,
It is energy saving.
4-8 layers of grid 14 are provided in main unit for dryer 13 as a further improvement of the utility model,.
The height of cavity layer 15 is 50-100mm as a further improvement of the utility model,.Silica dehydrator under this height
Grid 14 in device 12 can make the space utilization rate in main unit for dryer 13 be in optimal range.
Water purifier 6 includes shell 16 as a further improvement of the utility model, and it is defeated that 16 one end of shell is provided with water purifier
Enter end 17, the water purifier input terminal 17 is connected with the water inlet 7 of inlet pipeline, and it is defeated that 16 other end of shell is provided with water purifier
Outlet 18, the water purifier output end 18 are connected with the water inlet 9 of condenser pipe, and the inside of the shell 16 is from close to water inlet
7 are disposed with coarse filtration area 19, thin filtering area 20, magnetized filtering area 21 and ion-exchange area 22 to water outlet 10.This is practical
Novel high-efficiency condensation device is provided with the water purifier of scale removal effect, and the water purifier is provided with coarse filtration area 19, thin filtering area
20, magnetized filtering area 21 and ion-exchange area 22 can remove coarse solid particle in heat transferring medium, fine solid particles and again
Metal ion prevents that fouling occurs in the condenser pipe of condensing unit, improves the service life of equipment, guarantees the stabilization of heat exchange efficiency
Property.
Coarse filtration cavity 23, institute are provided between shell 16 and coarse filtration area 19 as a further improvement of the utility model,
It states and is provided with fine filtering cavity 24 between coarse filtration area 19 and thin filtering area 20.Case of water purifier 16 and thick mistake in the utility model
It is respectively arranged with coarse filtration cavity 23 and fine filtering cavity 24 between filter area 19, between coarse filtration area 19 and thin filtering, heat transferring medium is first
Preliminary coarse filtration is carried out into coarse filtration area 19 is crossed, coarse solid particle is blocked in the coarse filtration cavity 23 of 19 side of coarse filtration area
In, then heat transferring medium enters thin 20 fine filtering of filtering area, and tiny solid particle is blocked in thin filtering fine filtering cavity 24
On, this set energy dispersion solid particle makes water purifier be not easy to block in filtering area side deposition, improves condensation dress
The filter efficiency set guarantees efficient condensation effect.
To be connected with coarse filtration miscellaneous by conical collecting pipe 25 for 23 bottom of coarse filtration cavity as a further improvement of the utility model,
Matter collecting box 26,24 bottom of fine filtering cavity are connected with fine filtering impurity collecting box 27 by conical collecting pipe 25.Coarse filtration impurity
The receiving volume of collecting box 26 is greater than the thin receiving volume for considering impurity collecting box 27, in this way can effective categorised collection different size
Impurity, improve equipment cleaning, removal of impurities working efficiency.
Water purifier 6 further includes having from scale removal mechanism as a further improvement of the utility model, described from scale removal mechanism packet
Backflushing water intake pipe 28 and recoil outlet pipe 29 are included, the backflushing water intake pipe 28 is connected with 16 right end of shell, and recoil outlet pipe 29
It is connected with 16 left end of shell.Water purifier in the utility model is additionally provided with from scale removal mechanism, is rinsed by reverse flow, will
The scale adhered in coarse filtration area 19 and thin filtering area 20 is washed from, is peeled off, and falls into impurity collecting box, avoids replacement filtering area, drop
Low cost improves degree easy to operate.
Conical collecting pipe 25 includes cone-shaped collection bucket 30 and enrichment pipe 31, cone as a further improvement of the utility model,
The big end of shape collection bucket 30 is connected with coarse filtration cavity 23 or fine filtering cavity 24, and the small end of cone-shaped collection bucket 30 connects enrichment pipe
31, control valve is provided on enrichment pipe 31.It is provided with control valve on enrichment pipe 31, for controlling whether impurity falls into accordingly
Slightly, carefully in impurity collecting box.
Control valve is provided on backflushing water intake pipe 28 and recoil outlet pipe 29 as a further improvement of the utility model,.
The high-efficiency condensation device of the utility model can dehydrate, and improve the purity for the product that condensation is collected.
A kind of high-efficiency condensation device provided by the utility model is described in detail above.Tool used herein
Body embodiment is expounded the principles of the present invention and embodiment, and the explanation of above example is only intended to help to manage
Solve the method and its core concept of the utility model.It should be pointed out that for those skilled in the art, not
Under the premise of being detached from the utility model principle, several improvements and modifications can be made to this utility model, these improve and repair
Decorations are also fallen into the protection scope of the utility model claims.
Claims (10)
1. a kind of high-efficiency condensation device, it is characterised in that: including air inlet pipeline and inlet pipeline, successively set on the air inlet pipeline
It is equipped with drier and condensing tower, the air inlet of air inlet pipeline and the input terminal of drier connect, the output end of drier and condensation
The air intake of top of tower connects, and condensing tower lower part is provided with outlet pipe, and high-temperature gas is drained into next procedure by outlet pipe；Institute
It states and is disposed with water purifier and the condensing tower on inlet pipeline, the water inlet of inlet pipeline and the input terminal of water purifier connect
It connects, the water inlet for the spiral cold-finger being arranged in the output end and condensing tower of water purifier is connected, and the water outlet of spiral cold-finger will
Cooling water is discharged outside condensing tower；The condensation tower bottom is connected with collecting tank, and the drier is silica gel drier.
2. high-efficiency condensation device according to claim 1, it is characterised in that: the silica gel drier includes drier sheet
The input terminal of body, the main unit for dryer is connected with air inlet, the output end of main unit for dryer and enters gas at the top of condensing tower
Mouth is connected, and several layers grid is provided in main unit for dryer, silica dehydrator layer is provided on grid, described in adjacent two layers
A cavity layer is formed between grid.
3. high-efficiency condensation device according to claim 2, it is characterised in that: be provided with 4-8 layers in the main unit for dryer
Grid.
4. high-efficiency condensation device according to claim 2, it is characterised in that: the height of the cavity layer is 50-100mm.
5. high-efficiency condensation device according to claim 1, it is characterised in that: the water purifier includes shell, shell one end
It is provided with water purifier input terminal, the water purifier input terminal is connected with the water inlet of inlet pipeline, and the shell other end is provided with
Water purifier output end, the water purifier output end are connected with the water inlet of condenser pipe, and the inside of the shell is from close to water inlet
Mouth to water outlet is disposed with coarse filtration area, thin filtering area, magnetized filtering area and ion-exchange area.
6. high-efficiency condensation device according to claim 5, it is characterised in that: be provided between the shell and coarse filtration area
Coarse filtration cavity is provided with fine filtering cavity between the coarse filtration area and thin filtering area.
7. high-efficiency condensation device according to claim 6, it is characterised in that: the coarse filtration cavity bottom passes through cone-shaped collection
Pipe is connected with coarse filtration impurity collecting box, and the fine filtering cavity bottom is connected with fine filtering impurity collecting box by conical collecting pipe.
8. high-efficiency condensation device according to claim 1, it is characterised in that: the water purifier further includes having from scaler
Structure, described from scale removal mechanism includes backflushing water intake pipe and recoil outlet pipe, and the backflushing water intake pipe is connected with shell right end, instead
Water pipe is gone out to be connected with shell left end.
9. high-efficiency condensation device according to claim 7, it is characterised in that: the conical collecting pipe includes cone-shaped collection bucket
And enrichment pipe, the big end of cone-shaped collection bucket are connected with coarse filtration cavity or fine filtering cavity, the small end of cone-shaped collection bucket connects enrichment
It manages, is provided with control valve on enrichment pipe.
10. high-efficiency condensation device according to claim 8, it is characterised in that: the backflushing water intake pipe and recoil outlet pipe
On be provided with control valve.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201920067916.7U CN209451346U (en) | 2019-01-15 | 2019-01-15 | A kind of high-efficiency condensation device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201920067916.7U CN209451346U (en) | 2019-01-15 | 2019-01-15 | A kind of high-efficiency condensation device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN209451346U true CN209451346U (en) | 2019-10-01 |
Family
ID=68044679
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201920067916.7U Expired - Fee Related CN209451346U (en) | 2019-01-15 | 2019-01-15 | A kind of high-efficiency condensation device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN209451346U (en) |
-
2019
- 2019-01-15 CN CN201920067916.7U patent/CN209451346U/en not_active Expired - Fee Related
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20191001 Termination date: 20210115 |
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| CF01 | Termination of patent right due to non-payment of annual fee |