CN211782579U - Vacuum belt drying system - Google Patents
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- CN211782579U CN211782579U CN202020165000.8U CN202020165000U CN211782579U CN 211782579 U CN211782579 U CN 211782579U CN 202020165000 U CN202020165000 U CN 202020165000U CN 211782579 U CN211782579 U CN 211782579U
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- 238000001035 drying Methods 0.000 title claims abstract description 60
- 238000010438 heat treatment Methods 0.000 claims abstract description 73
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 30
- 239000007788 liquid Substances 0.000 claims description 26
- 230000007246 mechanism Effects 0.000 claims description 19
- 238000001816 cooling Methods 0.000 claims description 18
- 238000004891 communication Methods 0.000 claims description 10
- 239000000463 material Substances 0.000 abstract description 15
- 238000005265 energy consumption Methods 0.000 abstract description 5
- 238000007906 compression Methods 0.000 description 22
- 230000006835 compression Effects 0.000 description 21
- 230000001105 regulatory effect Effects 0.000 description 16
- 239000003245 coal Substances 0.000 description 8
- 239000003814 drug Substances 0.000 description 6
- 238000000034 method Methods 0.000 description 5
- 230000008569 process Effects 0.000 description 5
- 238000009833 condensation Methods 0.000 description 3
- 230000005494 condensation Effects 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- 238000001704 evaporation Methods 0.000 description 3
- 230000008020 evaporation Effects 0.000 description 3
- 238000002347 injection Methods 0.000 description 3
- 239000007924 injection Substances 0.000 description 3
- 230000001502 supplementing effect Effects 0.000 description 3
- 238000001291 vacuum drying Methods 0.000 description 3
- 239000010963 304 stainless steel Substances 0.000 description 2
- 229910000589 SAE 304 stainless steel Inorganic materials 0.000 description 2
- 238000004364 calculation method Methods 0.000 description 2
- 238000006243 chemical reaction Methods 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 238000007599 discharging Methods 0.000 description 2
- 238000006073 displacement reaction Methods 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 238000000926 separation method Methods 0.000 description 2
- 239000000243 solution Substances 0.000 description 2
- 238000001311 chemical methods and process Methods 0.000 description 1
- 230000009977 dual effect Effects 0.000 description 1
- 230000005611 electricity Effects 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 230000008676 import Effects 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000004321 preservation Methods 0.000 description 1
- 238000004064 recycling Methods 0.000 description 1
- 238000007789 sealing Methods 0.000 description 1
- 238000005507 spraying Methods 0.000 description 1
- 239000002918 waste heat Substances 0.000 description 1
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Abstract
The utility model relates to a drying equipment technical field discloses a vacuum belt drying system, include: the system comprises a vacuum belt dryer, a steam compressor and a steam ejector, wherein a heating zone is arranged inside the vacuum belt dryer; and a steam outlet of the vacuum belt dryer is communicated with an inlet of the steam compressor, an outlet of the steam compressor is communicated with a first steam inlet of the steam ejector, and a steam outlet of the steam ejector is communicated with the heating area. The vacuum belt drying system can recover secondary steam evaporated from materials in the drying process, and the secondary steam is compressed and enthalpy-increased twice through the steam compressor and the steam ejector in sequence, so that the steam temperature is increased to a preset state, and then the steam returns to the drying system to serve as heat source steam, the energy utilization rate of the vacuum belt drying system can be effectively improved, the energy consumption and the operation cost are greatly reduced, and compared with the traditional vacuum belt drying system, the energy consumption is reduced by more than 60%.
Description
Technical Field
The utility model relates to a drying equipment technical field especially relates to a vacuum belt drying system.
Background
The vacuum belt type dryer is contact type vacuum drying equipment in a continuous feeding and continuous discharging mode, and is widely applied to a traditional Chinese medicine extract drying process at home. Vacuum belt type drying is an advanced process for ensuring the drying quality of the traditional Chinese medicine extract, and can be widely popularized in traditional Chinese medicine production enterprises in China. However, the traditional vacuum belt dryer is driven by steam, so that the steam consumption is large, the running cost is high, and the development of a novel efficient energy-saving vacuum belt drying system tends to be great.
SUMMERY OF THE UTILITY MODEL
The embodiment of the utility model provides a vacuum belt drying system for solve or partially solve the huge problem of traditional vacuum belt dryer energy consumption.
The embodiment of the utility model provides a vacuum belt drying system, include: the system comprises a vacuum belt dryer, a steam compressor and a steam ejector, wherein a heating zone is arranged inside the vacuum belt dryer;
and a steam outlet of the vacuum belt dryer is communicated with an inlet of the steam compressor, an outlet of the steam compressor is communicated with a first steam inlet of the steam ejector, and a steam outlet of the steam ejector is communicated with the heating area.
On the basis of the technical scheme, the vacuum belt drying system further comprises a conveyor belt mechanism positioned inside the vacuum belt dryer, and the heating zone is correspondingly arranged below the conveyor belt mechanism.
On the basis of the technical scheme, the heating zone comprises a first heating zone and a second heating zone which are sequentially arranged along the conveying direction of the conveyor belt mechanism, the first heating zone is communicated with a steam outlet of the steam ejector, and the second heating zone is selectively communicated with the steam outlet of the steam ejector.
On the basis of the technical scheme, the second heating area is communicated with a hot water source.
On the basis of the technical scheme, a cooling area which is correspondingly arranged below the conveyor belt mechanism is further arranged in the vacuum belt dryer, and the cooling area is arranged close to the second heating area.
On the basis of the technical scheme, the first heating area, the second heating area and the cooling area are respectively and correspondingly provided with a first heating plate, a second heating plate and a cooling plate.
On the basis of the technical scheme, the vacuum belt type drying system further comprises a three-phase separator, a steam inlet of the three-phase separator is communicated with a steam outlet of the vacuum belt type dryer, and a steam outlet of the three-phase separator is communicated with an inlet of the steam compressor.
On the basis of the technical scheme, the vacuum belt type drying system further comprises a wire mesh filter, wherein an inlet of the wire mesh filter is communicated with a steam outlet of the three-phase separator, and an outlet of the wire mesh filter is communicated with an inlet of the steam compressor.
On the basis of the technical scheme, the vacuum belt type drying system further comprises a steam-liquid separator, a steam inlet of the steam-liquid separator is communicated with a steam outlet of the steam ejector, and a steam outlet of the steam-liquid separator is communicated with the heating area.
On the basis of the technical scheme, the vacuum belt drying system further comprises a condensate water tank and a condensate water pump, a condensate outlet of the vapor-liquid separator is communicated with a liquid inlet of the condensate water tank, a liquid outlet of the condensate water tank is communicated with an inlet of the condensate water pump, and an outlet of the condensate water pump is communicated with the steam compressor.
The embodiment of the utility model provides a pair of vacuum belt drying system, the secondary steam that the material evaporated among the recoverable drying process to loop through twice compression enthalpy addition of steam compressor and steam ejector, make steam temperature promote to the predetermined state after, return drying system and act as heat source steam. The vacuum belt drying system provided by the embodiment of the utility model can adjust the vacuum degree by the compressor under the novel double compression mode, the compressor can be adjusted in a frequency conversion stepless way, the accurate temperature control can be realized, and the quality of the traditional Chinese medicine extract is ensured; the secondary steam is compressed by double compression, so that the heat source temperature of the secondary steam can be greatly improved, the waste heat of the secondary steam generated by the vacuum cavity is recovered, and meanwhile, the vacuum power equipment of the traditional vacuum belt dryer is cancelled, so that the energy is saved by more than 60%.
Drawings
In order to more clearly illustrate the embodiments of the present invention or the technical solutions in the prior art, the drawings needed to be used in the description of the embodiments or the prior art will be briefly described below, and it is obvious that the drawings in the following description are some embodiments of the present invention, and for those skilled in the art, other drawings can be obtained according to these drawings without creative efforts.
Fig. 1 is a schematic structural diagram of a vacuum belt drying system according to an embodiment of the present invention.
Reference numerals:
1. a vacuum belt dryer; 2. a feeding mechanism; 3. a conveyor belt mechanism; 4. a first heating zone; 5. a second heating zone; 6. a cooling zone; 7. a dry material discharge mechanism; 8. a steam outlet of the vacuum belt dryer; 9. a first steam regulating valve; 10. a three-phase separator; 11. a first condensate regulating valve; 12. a second steam regulating valve; 13. a wire mesh filter; 14. a vapor compressor; 15. a steam ejector; 16. a third steam regulating valve; 17. a fourth steam regulating valve; 18. a vapor-liquid separator; 19. a second condensate regulating valve; 20. a condensate tank; 21. a condensate pump; 22. a fifth steam regulating valve; 23. a three-way valve; 24. a sixth steam regulating valve; 25. a first hot water regulating valve; 26. and a cold water regulating valve.
Detailed Description
In order to make the objects, technical solutions and advantages of the embodiments of the present invention clearer, the embodiments of the present invention will be clearly and completely described below with reference to the accompanying drawings in the embodiments of the present invention, and it is obvious that the described embodiments are some, but not all, embodiments of the present invention. Based on the embodiments in the present invention, all other embodiments obtained by a person skilled in the art without creative efforts belong to the protection scope of the present invention.
In the description of the present invention, it is to be noted that, unless otherwise explicitly specified or limited, the terms "mounted," "connected," and "connected" are to be construed broadly, and may be, for example, fixedly connected, detachably connected, or integrally connected; can be mechanically or electrically connected; they may be connected directly or indirectly through intervening media, or they may be interconnected between two elements. The specific meaning of the above terms in the present invention can be understood in specific cases to those skilled in the art.
In the operation process of the vacuum belt type drying system, the moisture of the materials in the dryer is evaporated at low temperature in a vacuum environment, the enthalpy value of the steam discharged by evaporation is low, and the value of direct recycling is not high. The part of steam is subjected to double-compression enthalpy increase through the steam compressor and the steam ejector and then is recycled, so that the steam consumption during the operation of the system can be reduced, the energy utilization rate of the system is effectively improved, and the operation cost is reduced.
Fig. 1 is the utility model discloses a vacuum belt drying system's of embodiment structural schematic diagram, as shown in fig. 1, the utility model discloses vacuum belt drying system, include: the device comprises a vacuum belt dryer 1, a steam compressor 14 and a steam ejector 15, wherein a heating zone is arranged inside the vacuum belt dryer 1;
the steam outlet 8 of the vacuum belt dryer is communicated with the inlet of a steam compressor 14, the outlet of the steam compressor 14 is communicated with a first steam inlet of a steam ejector 15, and the steam outlet of the steam ejector 15 is communicated with the heating zone.
The feeding mechanism 2 and the steam outlet 8 of the vacuum belt dryer are positioned above the vacuum belt dryer 1, and the dry material discharging mechanism 7 is arranged below the vacuum belt dryer 1. The second steam inlet of the steam injector 15 is connected to a third steam control valve 16.
The embodiment of the utility model provides a vacuum belt drying system, can retrieve the low temperature steam that the material produced in vacuum drying process, steam increases the enthalpy through the 14 compressions of steam compressor, improve the temperature and the pressure of steam, pass through steam ejector 15 again, mix the back compression injection with the high temperature steam that lets in newly in steam ejector 15, the steam that output temperature and pressure are higher sends into the zone of heating with the highly compressed steam of high temperature as the heat source at last, provide the heat and with the dry material of heat-conducting form for the zone of heating. This vacuum belt drying system can retrieve the secondary steam among the vacuum drying process, increases the enthalpy and utilizes again to the secondary steam pressurization through two compression modes, can effectively improve energy utilization, reduces the steam consumption among the drying process, reduces the energy consumption and the running cost of traditional vacuum belt drying system by a wide margin.
On the basis of the above-mentioned embodiment, the vacuum belt drying system further includes a conveyor belt mechanism 3 located inside the vacuum belt dryer 1, and the heating zone is correspondingly disposed below the conveyor belt mechanism 3.
Note that the conveyor belt mechanism 3 is horizontally arranged inside the vacuum belt dryer 1.
The embodiment of the utility model provides an in, the high temperature steam that mixes back compression injection with newly letting in steam ejector 15, the higher steam of output temperature and pressure send into the zone of heating with the highly compressed steam of high temperature as the heat source at last, provides the heat for the zone of heating and passes through the material that conveyor means 3 carried with the drying of heat-conducting form.
On the basis of the above embodiment, the heating zone includes the first heating zone 4 and the second heating zone 5 arranged in sequence along the conveying direction of the conveyor belt mechanism 3, the first heating zone 4 is communicated with the steam outlet of the steam injector 15, and the second heating zone 5 is selectively communicated with the steam outlet of the steam injector 15.
It should be noted that the second heating zone 5 is in communication with a hot water supply. Wherein the heating range of the first heating zone 4 may be larger than the heating range of the second heating zone 5.
In the embodiment of the utility model, high temperature high pressure steam in the steam ejector 15 carries the first zone of heating 4 in the vacuum belt dryer, provides the heat drying material, and the second zone of heating 5 lets in hot water and is used for heating the material. When the steam quantity supplied to the first heating zone 4 is excessive, the excessive high-temperature high-pressure steam can supply heat to the second heating zone 5.
On the basis of the above-described embodiment, the inside of the vacuum belt dryer 1 is further provided with a cooling zone 6 correspondingly arranged below the conveyor belt mechanism 3, the cooling zone 6 being arranged adjacent to the second heating zone 5.
The first heating zone 4, the second heating zone 5, and the cooling zone 6 are arranged in this order along the conveying direction of the conveyor mechanism 3. Wherein the cooling zone 6 is fed with cold water for cooling the material.
It is understood that the first heating zone 4, the second heating zone 5, and the cooling zone 6 are respectively installed with a first heating plate, a second heating plate, and a cooling plate. The cooling zone 6 is connected to a cold water supply via a cold water regulating valve 26, and the second heating zone 5 is connected to a hot water supply via a first hot water regulating valve 25.
On the basis of the above embodiment, the vacuum belt drying system further comprises a three-phase separator 10, wherein the steam inlet of the three-phase separator 10 is communicated with the steam outlet 8 of the vacuum belt dryer, and the steam outlet of the three-phase separator 10 is communicated with the inlet of the steam compressor 14.
In the embodiment of the present invention, the steam inlet of the three-phase separator 10 is communicated with the steam outlet 8 of the vacuum belt dryer through the first steam regulating valve 9, and the condensate outlet of the three-phase separator 10 is connected with the first condensate regulating valve 11.
On the basis of the above embodiment, the vacuum belt drying system further includes a wire mesh filter 13, an inlet of the wire mesh filter 13 is communicated with the steam outlet of the three-phase separator 10, and an outlet of the wire mesh filter 13 is communicated with an inlet of the steam compressor 14.
In the embodiment of the present invention, the inlet of the wire mesh filter 13 is communicated with the steam outlet of the three-phase separator 10 through the second steam regulating valve 12.
On the basis of the above embodiment, the vacuum belt drying system further includes a vapor-liquid separator 18, a vapor inlet of the vapor-liquid separator 18 is communicated with a vapor outlet of the steam ejector 15, and a vapor outlet of the vapor-liquid separator 18 is communicated with the heating zone.
The embodiment of the utility model provides an in, the steam inlet of vapour and liquid separator 18 passes through the steam outlet intercommunication of fourth steam control valve 17 with steam jet ejector 15, and the steam outlet and the fifth steam control valve 22 of vapour and liquid separator 18 communicate, and fifth steam control valve 22 communicates with the import of three-way valve 23, and the first export and the first zone of heating 4 of three-way valve 23 communicate, and the second export and the sixth steam control valve 24 of three-way valve 23 communicate, and sixth steam control valve 24 communicates with the second zone of heating 5.
On the basis of the above embodiment, the vacuum belt drying system further includes a condensate water tank 20 and a condensate water pump 21, a condensate outlet of the vapor-liquid separator 18 is communicated with a liquid inlet of the condensate water tank 20, a liquid outlet of the condensate water tank 20 is communicated with an inlet of the condensate water pump 21, and an outlet of the condensate water pump 21 is communicated with the vapor compressor 14.
In the embodiment of the present invention, the condensate outlet of the vapor-liquid separator 18 is communicated with the inlet of the condensate water tank 20 through the second condensate regulating valve 19.
The embodiment of the utility model provides a vacuum belt drying system, in vacuum belt drying process, the steam that the moisture evaporation of material produced in vacuum belt dryer 1 gets into three-phase separator 10 under vapor compressor 14's pressure effect earlier, the liquid discharge system of separation, steam after the separation filters through wire filter 13, steam after the filtration increases the enthalpy through vapor compressor 14 compression, then mix with the high-temperature steam of newly-supplied in getting into steam ejector 15, further improve the temperature and the pressure of steam, then high-temperature highly compressed steam gets into vapour and liquid separator 18, liquid in the steam gets into condensation water pitcher 20, condensate in condensation water pitcher 20 provides vapor compressor 14 under condensate pump 21's effect, guarantee its normal operating; the high-temperature high-pressure steam in the steam-liquid separator 18 is conveyed to the first heating plate in the vacuum belt dryer 1 to provide heat for drying the materials, and hot water and cold water are respectively introduced into the second heating plate and the cooling plate to heat and cool the materials. When the amount of steam supplied to the first heating plate is excessive, the excessive high-temperature and high-pressure steam may supply heat to the second heating plate.
The example conditions were as follows:
the original vacuum belt dryer of the embodiment (60 m)2) Drying the traditional Chinese medicine extract, wherein the evaporation water amount in the drying process is 50kg/H, the steam consumption of the vacuum belt dryer is 75kg/H, and the power consumption of the system is 29 kW.H/H.
Local energy prices: the average price of steam is 170 yuan/ton, and the unit price of an external wire (10kV) is 0.54 yuan/degree. Saving standard coal conversion: the equivalent heat of 1 kW.h electricity is 0.35kg standard coal; the equivalent heat of 1kg of steam was 0.145kg of standard coal.
Description of the main equipment:
a three-phase separator: the vertical spraying type is characterized in that the cylinder body is made of 304 stainless steel, the thickness of the heat-insulating layer is 50mm, the thickness of the wire mesh is 50mm, and the size phi is 400x1500 mm.
A wire mesh filter: DN 200.
Condensation water tank: the horizontal type vacuum furnace is characterized in that the cylinder body is made of 304 stainless steel, the thickness of the heat-insulating layer is 50mm, and the size phi of the heat-insulating layer is 400x1500 mm.
A condensate pump: a chemical process pump with double sealing type and 304 materials, the power is 1.5kW, and the flow is 1.5m3/h。
Vapor compressor feed pump: flow rate of 1.5m3H, power 1.5 kW.
An oil tank: the vertical type heat preservation layer has the thickness of 50mm and the diameter of 300x400 mm.
Energy-saving calculation:
1. original equipment: the low-temperature steam evaporated in the operation process of the traditional Chinese medicine extract drying system is not recycled, and the steam consumption of matched equipment and the power consumption of a vacuum pump are mainly considered in energy-saving calculation.
Operating cost per hour: 0.075 x 170+29 x 0.54 ═ 28.41 yuan
Standard coal consumption per hour: 75 × 0.145+29 × 0.35 ═ 21.025kg
2. Mechanical compression alone increases enthalpy: recovering 50kg/h low temperature steam (average 40 deg.C) evaporated during drying process of Chinese medicinal extract, compressing by vapor compressor to increase enthalpy to 116 deg.C, directly delivering high temperature and high pressure steam to the first heating plate, and additionally supplementing 25kg/h high temperature steam to the first heating plate. The specific parameters of the vapor compressor are as follows: compressor displacement 20m3The flow is 50kg/h, the steam absorbing and exhausting temperature is 40-116 ℃, the actual power consumption is 45kW/h during operation, and the power distribution machine is 55 kW.
Operating cost per hour: 0.025 × 170+45 × 0.54 ═ 28.55 yuan
Standard coal consumption per hour: 25 × 0.145+45 × 0.35 ═ 19.375kg
3. Dual compression mode enthalpy gain: the recovered 50kg/h low-temperature steam (average 40 ℃) still passes through the steam compressor, the compression enthalpy is increased to 90 ℃, a steam ejector is additionally arranged at the outlet of the steam compressor, the heat supplementing steam is used as the working steam of the steam ejector, and the secondary steam pressurization of the belt dryer is realized without additionally increasing the energy consumption. The working steam of the steam ejector adopts the heat supplementing steam of the system, the injection coefficient is 2, the compression ratio of the steam ejector pump is 2.5, the supplemented steam quantity is 25kg/h, the working steam temperature is 170 ℃ (the pressure is 800kpa), 75kg/h mixed steam is generated at the outlet of the ejector, and the mixed steam temperature is 116 ℃ (the pressure is 175 kpa). The specific parameters of the vapor compressor are as follows: compressor displacement of 20m3The flow is 50kg/h, the steam absorbing and exhausting temperature is 40-90 ℃, the actual power consumption is 12kW/h, and the power distribution machine is 15 kW.
Operating cost per hour: 0.025 × 170+12 × 0.54 ═ 10.73 yuan
Standard coal consumption per hour: 25 × 0.145+12 × 0.35 ═ 7.825kg
TABLE 1 energy-saving statistical table
As can be seen from Table 1, the steam consumption per unit time of the single mechanical compression mode is reduced by 66.7% compared with that of the original equipment, but the low-temperature steam is compressed to 116 ℃ only by means of increasing enthalpy of the compression of the steam compressor, the pressure ratio of the compressor is too large, the shaft power is too high, and the actual power consumption of the steam compressor is too large; the system operating cost of the single mechanical compression mode is almost equal to the original system operating cost, but the standard coal can be saved by 8 percent. Therefore, the energy-saving cost-reducing effect of the single mechanical compression mode is not obvious.
The steam consumption per unit time of the double-compression-mode vacuum belt type drying system is also reduced by 66.7 percent compared with that of the original equipment; the operating cost of the double compression modes is reduced by 62.4 percent compared with that of a single mechanical compression mode and is reduced by 62.2 percent compared with that of the original system; the standard coal saving of the double compression modes is saved by 59.6 percent compared with the single mechanical compression mode and is saved by 62.8 percent compared with the original system. Therefore, according to the present embodiment: the enthalpy-increasing energy-saving vacuum belt type drying system based on the double compression modes can greatly reduce the extra steam consumption during the operation of the system, effectively improve the energy utilization rate of the system and reduce the operation cost.
The above description is only a preferred embodiment of the present invention, and should not be taken as limiting the invention, and any modifications, equivalent replacements, improvements, etc. made within the spirit and principle of the present invention should be included in the protection scope of the present invention.
Claims (10)
1. A vacuum belt drying system, comprising: the system comprises a vacuum belt dryer, a steam compressor and a steam ejector, wherein a heating zone is arranged inside the vacuum belt dryer;
and a steam outlet of the vacuum belt dryer is communicated with an inlet of the steam compressor, an outlet of the steam compressor is communicated with a first steam inlet of the steam ejector, and a steam outlet of the steam ejector is communicated with the heating area.
2. The vacuum belt drying system of claim 1, further comprising a conveyor mechanism located inside the vacuum belt dryer, the heating zone being correspondingly disposed below the conveyor mechanism.
3. The vacuum belt drying system of claim 2, wherein the heating zone comprises a first heating zone and a second heating zone arranged in sequence along the conveying direction of the conveyor belt mechanism, the first heating zone being in communication with the steam outlet of the steam injector, the second heating zone being in selective communication with the steam outlet of the steam injector.
4. The vacuum belt drying system of claim 3, wherein the second heating zone is in communication with a source of hot water.
5. The vacuum belt drying system of claim 3, wherein the interior of the vacuum belt dryer is further provided with a cooling zone disposed correspondingly below the conveyor belt mechanism, the cooling zone being disposed adjacent to the second heating zone.
6. The vacuum belt drying system of claim 5, wherein the first heating zone, the second heating zone, and the cooling zone are respectively installed with a first heating plate, a second heating plate, and a cooling plate.
7. The vacuum belt drying system of any one of claims 1 to 6, further comprising a three-phase separator, a vapor inlet of the three-phase separator being in communication with a vapor outlet of the vacuum belt dryer, a vapor outlet of the three-phase separator being in communication with an inlet of the vapor compressor.
8. The vacuum belt drying system of claim 7, further comprising a wire mesh filter, an inlet of the wire mesh filter being in communication with the vapor outlet of the three-phase separator, an outlet of the wire mesh filter being in communication with an inlet of the vapor compressor.
9. The vacuum belt drying system according to any one of claims 1 to 6, further comprising a vapor-liquid separator, a vapor inlet of the vapor-liquid separator being in communication with a vapor outlet of the steam ejector, a vapor outlet of the vapor-liquid separator being in communication with the heating zone.
10. The vacuum belt drying system of claim 9, further comprising a condensate tank and a condensate pump, wherein a condensate outlet of the vapor-liquid separator is communicated with a liquid inlet of the condensate tank, a liquid outlet of the condensate tank is communicated with an inlet of the condensate pump, and an outlet of the condensate pump is communicated with the vapor compressor.
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| CN202020165000.8U CN211782579U (en) | 2020-02-12 | 2020-02-12 | Vacuum belt drying system |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111174556A (en) * | 2020-02-12 | 2020-05-19 | 中国科学院理化技术研究所 | Vacuum belt drying system |
| CN112539637A (en) * | 2020-12-11 | 2021-03-23 | 江苏长能节能新材料科技有限公司 | Method for continuously drying hexamethylol melamine |
-
2020
- 2020-02-12 CN CN202020165000.8U patent/CN211782579U/en active Active
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111174556A (en) * | 2020-02-12 | 2020-05-19 | 中国科学院理化技术研究所 | Vacuum belt drying system |
| CN112539637A (en) * | 2020-12-11 | 2021-03-23 | 江苏长能节能新材料科技有限公司 | Method for continuously drying hexamethylol melamine |
| CN112539637B (en) * | 2020-12-11 | 2022-06-21 | 江苏长能节能新材料科技有限公司 | Method for continuously drying hexamethylol melamine |
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