CN208313099U - A kind of afterheat utilizing system during glycerol production - Google Patents
A kind of afterheat utilizing system during glycerol production Download PDFInfo
- Publication number
- CN208313099U CN208313099U CN201820605436.7U CN201820605436U CN208313099U CN 208313099 U CN208313099 U CN 208313099U CN 201820605436 U CN201820605436 U CN 201820605436U CN 208313099 U CN208313099 U CN 208313099U
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- Prior art keywords
- water
- pipe
- water tank
- outlet
- heat
- 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.)
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- PEDCQBHIVMGVHV-UHFFFAOYSA-N Glycerine Chemical compound OCC(O)CO PEDCQBHIVMGVHV-UHFFFAOYSA-N 0.000 title claims abstract description 101
- 238000004519 manufacturing process Methods 0.000 title claims abstract description 21
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 181
- 241000220317 Rosa Species 0.000 claims abstract description 21
- 238000009833 condensation Methods 0.000 claims abstract description 18
- 230000005494 condensation Effects 0.000 claims abstract description 18
- 238000009825 accumulation Methods 0.000 claims abstract description 16
- 238000004821 distillation Methods 0.000 claims abstract description 14
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims abstract description 11
- 229910052799 carbon Inorganic materials 0.000 claims abstract description 11
- 230000010412 perfusion Effects 0.000 claims description 19
- 239000007921 spray Substances 0.000 claims description 13
- 239000006096 absorbing agent Substances 0.000 claims description 9
- JEGUKCSWCFPDGT-UHFFFAOYSA-N h2o hydrate Chemical compound O.O JEGUKCSWCFPDGT-UHFFFAOYSA-N 0.000 claims description 6
- 238000009413 insulation Methods 0.000 claims description 5
- 238000001914 filtration Methods 0.000 claims description 4
- 235000011187 glycerol Nutrition 0.000 abstract description 30
- 238000004064 recycling Methods 0.000 abstract description 2
- 239000007789 gas Substances 0.000 description 11
- 238000010586 diagram Methods 0.000 description 4
- 238000010438 heat treatment Methods 0.000 description 3
- 238000000034 method Methods 0.000 description 3
- 230000000694 effects Effects 0.000 description 2
- 229920002160 Celluloid Polymers 0.000 description 1
- 241000208125 Nicotiana Species 0.000 description 1
- 235000002637 Nicotiana tabacum Nutrition 0.000 description 1
- 229920000180 alkyd Polymers 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 235000013361 beverage Nutrition 0.000 description 1
- 235000009508 confectionery Nutrition 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 239000003814 drug Substances 0.000 description 1
- 238000004043 dyeing Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 239000002360 explosive Substances 0.000 description 1
- 235000013305 food Nutrition 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 229920002635 polyurethane Polymers 0.000 description 1
- 239000004814 polyurethane Substances 0.000 description 1
- 239000004753 textile Substances 0.000 description 1
- 238000009834 vaporization Methods 0.000 description 1
- 230000008016 vaporization Effects 0.000 description 1
- 239000002918 waste heat Substances 0.000 description 1
Classifications
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
- Y02E60/14—Thermal energy storage
Landscapes
- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
Abstract
The utility model discloses the afterheat utilizing system during a kind of glycerol production, including distillation still, water heat accumulation apparatus, heat exchanger, vapour condensation device, Rose Box and water tank, the distillation still is equipped with the first escape pipe, and the first escape pipe connects water heat accumulation apparatus.Afterheat utilizing system during this set glycerol production is divided into two parts, the glycerol steam of first part passes to water heat accumulation apparatus by the first escape pipe, water in water tank is heated, the exhaust gas to turn cold is transferred to outside by the processing of active carbon layer, so that not polluting outside air, the hot water delivery in water tank is to heat exchanger, pass through heat exchange action, so that the cold water outside heat exchanger is become hot water, is easy to use, ensure that not wasting for the energy；Second part makes glycerin vapor condensation become water by vapour condensation device, and water again into water tank, provides water source for first part, reach the recycling of water after filter device is handled.
Description
Technical field
Afterheat utilizing system the utility model relates to field of waste heat utilization, during specifically a kind of glycerol production.
Background technique
Glycerol is also known as glycerine, is a kind of thick liquid, pleasantly sweet, so referred to as glycerol；Can and water with arbitrarily than miscible,
There is strong hygroscopicity, is important basic organic.The purposes of glycerol is very extensive, is mainly used for medicine, makeup
Product, alkyd resin, tobacco, food, beverage, polyurethanes, celluloid, explosive, textile printing and dyeing etc..About 1700
Multiple use.
In the production process of glycerol, after crude glycerine enters distillation still, glycerol vaporization enters cooling tower and condenses, in this process
In, the higher heat of glycerol steam is lost in vain, is all undesirable no matter in terms of economic aspect or environmental protection.
Therefore, those skilled in the art provide the afterheat utilizing system during a kind of glycerol production, above-mentioned to solve
The problem of being proposed in background technique.
Summary of the invention
The purpose of this utility model is to provide the afterheat utilizing systems during a kind of glycerol production, to solve above-mentioned back
The problem of being proposed in scape technology.
To achieve the above object, the utility model provides the following technical solutions:
A kind of afterheat utilizing system during glycerol production, including distillation still, water heat accumulation apparatus, heat exchanger, steam
Condensing unit, Rose Box and water tank, the lower end of the distillation still are equipped with the first escape pipe, the water heat accumulation apparatus upper end be equipped with into
Port, the upper end of the air inlet are connected with the first escape pipe, and the water heat accumulation apparatus includes water tank and inner casing, the water storage
Chamber interior wall is equipped with insulating layer, and the water tank is connected by pendant with inner casing, and the other end of gas outlet is connected with inner casing, institute
It states inner housing inner and is equipped with absorber plate, pass through heat-conducting plate between the absorber plate and connect, heat conducting pipe, institute are connected on the outside of the heat-conducting plate
It states the heat conducting pipe other end to extend to inside water tank, the inner casing side connects gas outlet, and the gas outlet extends to water tank
Outside, the side of the water tank are equipped with water inlet, and water inlet connects one end of water inlet pipe, the other end connection of the water inlet pipe
One end of water tank；
The other side of the water tank is equipped with water outlet, and the water outlet connects one end of outlet pipe, the outlet pipe
The other end is connected with the water inlet of heat exchanger, and the water outlet of the heat exchanger is connected with one end of circulation pipe, the circulation
It is connected inside the other end of pipe and water tank, upper end, which is equipped with, on the left of the heat exchanger uses water water inlet pipe, and the heat exchanger is left
Side lower end, which is equipped with, uses water outlet pipe, and described passed through with water water inlet pipe is connected inside heat exchanger with water outlet pipe, the distillation
The kettle other side is equipped with the second escape pipe, the air inlet of the second escape pipe connection vapour condensation device, the steam condensation dress
The water outlet set is connected with perfusion tube, and water valve is equipped in the middle part of the perfusion tube, and the perfusion tube connects pump intake, the water
The water outlet of pump connects the water inlet of Rose Box by perfusion tube, and the water outlet of the Rose Box connects the another of water tank by water pipe
One end.
The vapour condensation device includes shell, and the enclosure interior is equipped with thermal insulation layer, and the shell upper end is equipped with blower,
The shell lower end is equipped with sink, and the enclosure interior upper end is equipped with water collection device, and the water collection device passes through U-tube and sink phase
Even, condensate pump is equipped with inside the U-tube, the water collection device lower end is equipped with division box, the division box side wall connection
Spray head, the inner walls are equipped with condenser, and the inside of the condenser is equipped with condenser pipe, the inlet end of the condenser pipe and the
Two escape pipes are connected, and the other end of the condenser pipe is connected with perfusion tube.
The Rose Box includes cabinet, water outlet and water inlet, is respectively equipped with first from top to bottom inside the Rose Box
Filter layer, active carbon layer and the second filter layer, first filter layer and the second filter layer specification are identical.
The spray head quantity is at least four, and spray head is equally arranged in division box lower end.
The end of the gas outlet is provided with active carbon net.
As a further solution of the present invention: the vapour condensation device includes shell, and the shell, the shell
Inside is equipped with thermal insulation layer, and the shell upper end is equipped with blower, and the shell lower end is equipped with sink, and the enclosure interior upper end is equipped with
Water collection device, the water collection device are connected by U-tube with sink, and the water collection device lower end is equipped with division box, the division box
Side wall connects spray head, and the inner walls are equipped with condenser, and the inside of the condenser is equipped with condenser pipe, and the one of the condenser pipe
End is connected with escape pipe, and the other end of the U-tube is connected with perfusion tube.
The Rose Box includes cabinet as a further solution of the present invention, and case is equipped with inside the Rose Box
The water inlet of body, water outlet and water inlet, the Rose Box is connected by perfusion tube with the water outlet of water pump, the Rose Box
Water outlet be connected by the other end of water pipe and water tank, the first filtering is respectively equipped with inside the Rose Box from top to bottom
Layer, active carbon layer and the second filter layer, first filter layer and the second filter layer specification are identical.
The spray head quantity is at least four as a further solution of the present invention, and spray head is spaced set.
Active carbon net is provided at the top of the gas outlet as a further solution of the present invention,.
Compared with prior art, the utility model has the beneficial effects that the utility model designs rationally in structure, use
Getting up easy to operate, practicability is very high, and the afterheat utilizing system during this set glycerol production is divided into two parts, and first
Partial glycerol steam passes to water heat accumulation apparatus by the first escape pipe, heats to the water in water tank, and what is turned cold is useless
Gas is transferred to outside by the processing of active carbon layer, so that not polluting outside air, the hot water delivery in water tank is handed over to heat
It changes planes, by heat exchange action, the cold water outside heat exchanger is made to become hot water, be easy to use, ensure that not wasting for the energy；
Second part makes glycerin vapor condensation become water, water arrives again after filter device is handled by vapour condensation device
In water tank, water source is provided for first part, reaches the recycling of water.
Detailed description of the invention
Fig. 1 is a kind of structural schematic diagram of the afterheat utilizing system during glycerol production.
Fig. 2 be a kind of glycerol production during afterheat utilizing system in water heat accumulation apparatus structural schematic diagram.
Fig. 3 be a kind of glycerol production during afterheat utilizing system in vapour condensation device structural schematic diagram.
Fig. 4 be a kind of glycerol production during UTILIZATION OF VESIDUAL HEAT IN in Rose Box structural schematic diagram.
In figure: distillation still 1, the first escape pipe 2, air inlet 3, inner casing 4, heat conducting pipe 5, water tank 6, water outlet 7, heat-conducting plate
8, absorber plate 9, water heat accumulation apparatus 10, air inlet pipe 11, water inlet 12, gas outlet 13, insulating layer 14, outlet pipe 15, heat exchanger
16, with water outlet pipe 17, with water water inlet pipe 18, circulation pipe 19, water tank 20, water pipe 21, the second escape pipe 22, vapour condensation device
23, spray head 2301, blower 2302, division box 2303, water collection device 2304, condenser pipe 2305, U-tube 2306, thermal insulation layer 2307,
Sink 2308, condenser 2309, shell 2310, condensate pump 2311, water valve 24, water pump 25, Rose Box 26, the first filter layer
2601, active carbon layer 2602, the second filter layer 2603, cabinet 2604, perfusion tube 27.
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. 1~4, in the utility model embodiment, a kind of afterheat utilizing system during glycerol production, including
Distillation still 1, water heat accumulation apparatus 10, heat exchanger 16, vapour condensation device 23, Rose Box 26 and water tank 20, the distillation still 1
Lower end is equipped with the first escape pipe 2, and 10 upper end of water heat accumulation apparatus is equipped with air inlet 3, and the upper end of the air inlet 3 and first goes out
Tracheae 2 is connected, and the water heat accumulation apparatus 10 includes water tank 6 and inner casing 4, and 6 inner wall of water tank is equipped with insulating layer 14, described
Water tank 6 is connected by pendant with inner casing 4, and the other end of gas outlet 13 is connected with inner casing 4, is equipped with inside the inner casing 4
Absorber plate 9 is connected by heat-conducting plate 8 between the absorber plate 9, and heat conducting pipe 5, the heat conducting pipe are connected on the outside of the heat-conducting plate 8
5 other ends extend to inside water tank 6, and 4 side of inner casing connects gas outlet 13, and the gas outlet 13 extends to water tank 6
Outside, the side of the water tank 6 are equipped with water inlet 12, and water inlet 12 connects one end of water inlet pipe 11, the water inlet pipe 11
One end of other end connection water tank 20；
The other side of the water tank 6 is equipped with water outlet 7, and the water outlet 7 connects one end of outlet pipe 15, the water outlet
The other end of pipe 15 is connected with the water inlet of heat exchanger 16, one end phase of the water outlet and circulation pipe 19 of the heat exchanger 16
Even, it is connected inside the other end and water tank 6 of the circulation pipe 19, the 16 left side upper end of heat exchanger, which is equipped with, uses water water inlet pipe
18, the 16 left side lower end of heat exchanger, which is equipped with, uses water outlet pipe 17, described to be passed through inside heat exchanger 16 with water water inlet pipe 18
It is connected with water outlet pipe 17,1 other side of distillation still is equipped with the second escape pipe 22, and second escape pipe 22 connects steam
The water outlet of the air inlet of condensing unit 23, the vapour condensation device 23 is connected with perfusion tube 27,27 middle part of perfusion tube
Equipped with water valve 24, the perfusion tube 27 connects 25 water inlet of water pump, and the water outlet of the water pump 25 was connected by perfusion tube 27
The water inlet of filter box 26, the water outlet of the Rose Box 26 connect the other end of water tank 20 by water pipe 21.
The vapour condensation device 23 includes shell 2310, is equipped with thermal insulation layer 2307, the shell inside the shell 2310
2310 upper end of body is equipped with blower 2302, and 2310 lower end of shell is equipped with sink 2308, and 2310 inner upper end of shell is equipped with
Water collection device 2304, the water collection device 2304 are connected by U-tube 2306 with sink 2308, and condensed water is equipped with inside the U-tube
Pump 2311,2304 lower end of water collection device are equipped with division box 2303, and 2303 side wall of division box connects spray head 2301, institute
2310 inner wall of shell is stated equipped with condenser 2309, the inside of the condenser 2309 is equipped with condenser pipe 2305, the condenser pipe
2305 inlet end is connected with the second escape pipe 22, and the other end of the condenser pipe 2305 is connected with perfusion tube 27.
The Rose Box 26 includes cabinet 2604, water outlet and water inlet, is distinguished from top to bottom inside the Rose Box 26
Equipped with the first filter layer 2601, active carbon layer 2602 and the second filter layer 2603, first filter layer 2601 and the second filtering
2603 specification of layer are identical.
2301 quantity of spray head is at least four, and spray head 2301 is equally arranged in division box lower end.
The end of the gas outlet 13 is provided with active carbon net.
The working principle of the utility model is:
The utility model relates to the afterheat utilizing systems during a kind of glycerol production, are steamed by the glycerol in distillation still 1
Vapour is transferred to two escape pipes respectively, is transferred in water heat accumulation apparatus 10 by the first escape pipe 2, and the heat of glycerin vapor provides
To the absorber plate 9 in inner casing 4, the heat in absorber plate 9 is passed in heat-conducting plate 8, and heat-conducting plate 8, which is transferred to, is placed in 4 inner wall of inner casing
In heat conducting pipe 5, heat the water resource in water tank 6, the water after heating enters in heat exchanger 16 by outlet pipe 15, passes through
The effect of heat exchange makes external cold water heating, facilitates people's normal use hot water, and the cold water in heat exchanger 16 then weighs
It newly returns in water tank 6 and continues circulating-heating use；Enter vapour condensation device 23 by the glycerin vapor of the second escape pipe 22
In, so that the glycerin vapor in condenser pipe 2305 is condensed into water by the effect of condenser 2309, water was flowed by perfusion tube 27
Device 26 is filtered, is filtered, finally flows into water tank 20, water tank 20 also provides water source simultaneously for water tank 6, to accomplish following for water
Ring uses.
It is obvious to a person skilled in the art that the present invention is not limited to the details of the above exemplary embodiments, and
And without departing substantially from the spirit or essential attributes of the utility model, it can realize that this is practical new in other specific forms
Type.Therefore, in all respects, the present embodiments are to be considered as illustrative and not restrictive, this is practical new
The range of type is indicated by the appended claims rather than the foregoing description, it is intended that containing for the equivalent requirements of the claims will be fallen in
All changes in justice and range are embraced therein.It should not treat any reference in the claims as limiting
Related claim.
In addition, it should be understood that although this specification is described in terms of embodiments, but not each embodiment is only wrapped
Containing an independent technical solution, this description of the specification is merely for the sake of clarity, and those skilled in the art should
It considers the specification as a whole, the technical solutions in the various embodiments may also be suitably combined, forms those skilled in the art
The other embodiments being understood that.
Claims (5)
1. the afterheat utilizing system during a kind of glycerol production, including distillation still (1), water heat accumulation apparatus (10), heat exchanger
(16), vapour condensation device (23), Rose Box (26) and water tank (20), it is characterised in that: the lower end of the distillation still (1) is equipped with
First escape pipe (2), water heat accumulation apparatus (10) upper end are equipped with air inlet (3), and the upper end and first of the air inlet (3) goes out
Tracheae (2) is connected, and the water heat accumulation apparatus (10) includes water tank (6) and inner casing (4), and water tank (6) inner wall, which is equipped with, to be protected
Warm layer (14), the water tank (6) are connected by pendant with inner casing (4), and the other end of gas outlet (13) is connected with inner casing (4)
It connects, is equipped with absorber plate (9) inside the inner casing (4), connected between the absorber plate (9) by heat-conducting plate (8), the heat-conducting plate
(8) outside connects heat conducting pipe (5), and heat conducting pipe (5) other end extends to water tank (6) inside, and inner casing (4) side connects
It picks out port (13), the gas outlet (13) extends to water tank (6) outside, and the side of the water tank (6) is equipped with water inlet
(12), one end of water inlet (12) connection water inlet pipe (11), one end of other end connection water tank (20) of the water inlet pipe (11)；
The other side of the water tank (6) is equipped with water outlet (7), one end of water outlet (7) connection outlet pipe (15), described
The other end of outlet pipe (15) is connected with the water inlet of heat exchanger (16), the water outlet and circulation pipe of the heat exchanger (16)
(19) one end is connected, and is connected inside the other end and water tank (6) of the circulation pipe (19), on the left of the heat exchanger (16)
Upper end, which is equipped with, uses water water inlet pipe (18), and lower end, which is equipped with, on the left of the heat exchanger (16) uses water outlet pipe (17), it is described with water into
Water pipe (18), which passes through, to be connected inside heat exchanger (16) with water outlet pipe (17), and distillation still (1) other side is equipped with second
Escape pipe (22), the air inlet of the second escape pipe (22) connection vapour condensation device (23), the vapour condensation device
(23) water outlet is connected with perfusion tube (27), is equipped with water valve (24) in the middle part of the perfusion tube (27), and the perfusion tube (27) is even
Water pump (25) water inlet, water inlet of the water outlet of the water pump (25) by perfusion tube (27) connection Rose Box (26), institute
The water outlet for stating Rose Box (26) passes through the other end of water pipe (21) connection water tank (20).
2. the afterheat utilizing system during a kind of glycerol production according to claim 1, it is characterised in that: the steam
Condensing unit (23) includes shell (2310), is equipped with thermal insulation layer (2307) inside the shell (2310), the shell (2310)
Upper end is equipped with blower (2302), and shell (2310) lower end is equipped with sink (2308), and shell (2310) inner upper end is set
Have water collection device (2304), the water collection device (2304) is connected by U-tube (2306) with sink (2308), inside the U-tube
Equipped with condensate pump (2311), water collection device (2304) lower end is equipped with division box (2303), the division box (2303)
Side wall connects spray head (2301), and shell (2310) inner wall is equipped with condenser (2309), the inside of the condenser (2309)
Equipped with condenser pipe (2305), the inlet end of the condenser pipe (2305) is connected with the second escape pipe (22), the condenser pipe
(2305) the other end is connected with perfusion tube (27).
3. the afterheat utilizing system during a kind of glycerol production according to claim 1, it is characterised in that: the filtering
Case (26) includes cabinet (2604), water outlet and water inlet, is respectively equipped with the first mistake from top to bottom inside the Rose Box (26)
Filtering layer (2601), active carbon layer (2602) and the second filter layer (2603), first filter layer (2601) and the second filter layer
(2603) specification is identical.
4. the afterheat utilizing system during a kind of glycerol production according to claim 2, it is characterised in that: the spray head
(2301) quantity is at least four, and spray head (2301) is equally arranged in division box (2303) lower end.
5. the afterheat utilizing system during a kind of glycerol production according to claim 1, it is characterised in that: the outlet
The end of mouth (13) is provided with active carbon net.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201820605436.7U CN208313099U (en) | 2018-04-26 | 2018-04-26 | A kind of afterheat utilizing system during glycerol production |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201820605436.7U CN208313099U (en) | 2018-04-26 | 2018-04-26 | A kind of afterheat utilizing system during glycerol production |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN208313099U true CN208313099U (en) | 2019-01-01 |
Family
ID=64714477
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201820605436.7U Expired - Fee Related CN208313099U (en) | 2018-04-26 | 2018-04-26 | A kind of afterheat utilizing system during glycerol production |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN208313099U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111141157A (en) * | 2019-12-07 | 2020-05-12 | 安徽康宁油脂科技有限公司 | Industrial grade glycerine processing is with glycerine steam condensation collection device |
-
2018
- 2018-04-26 CN CN201820605436.7U patent/CN208313099U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111141157A (en) * | 2019-12-07 | 2020-05-12 | 安徽康宁油脂科技有限公司 | Industrial grade glycerine processing is with glycerine steam condensation collection device |
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Granted publication date: 20190101 |