CN211383841U - Practical economic benefits and social benefits enrichment facility - Google Patents
Practical economic benefits and social benefits enrichment facility Download PDFInfo
- Publication number
- CN211383841U CN211383841U CN201922311916.XU CN201922311916U CN211383841U CN 211383841 U CN211383841 U CN 211383841U CN 201922311916 U CN201922311916 U CN 201922311916U CN 211383841 U CN211383841 U CN 211383841U
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- heater
- pipe
- effect
- steam
- evaporator
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- Expired - Fee Related
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- 238000007599 discharging Methods 0.000 claims abstract description 9
- 239000002699 waste material Substances 0.000 claims description 30
- 230000000694 effects Effects 0.000 claims description 21
- 238000000034 method Methods 0.000 claims description 2
- 238000009413 insulation Methods 0.000 claims 3
- 238000004519 manufacturing process Methods 0.000 abstract description 5
- 238000006243 chemical reaction Methods 0.000 abstract description 3
- 238000010438 heat treatment Methods 0.000 abstract description 2
- 239000000463 material Substances 0.000 description 4
- 230000008020 evaporation Effects 0.000 description 3
- 238000001704 evaporation Methods 0.000 description 3
- 238000012986 modification Methods 0.000 description 3
- 230000004048 modification Effects 0.000 description 3
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 3
- 238000004321 preservation Methods 0.000 description 2
- 239000002918 waste heat Substances 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 1
- 239000012141 concentrate Substances 0.000 description 1
- 238000009833 condensation Methods 0.000 description 1
- 230000005494 condensation Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000004134 energy conservation Methods 0.000 description 1
- 238000011010 flushing procedure Methods 0.000 description 1
- 230000002265 prevention Effects 0.000 description 1
- 238000005070 sampling Methods 0.000 description 1
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- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
Abstract
The utility model discloses a practical double-effect concentration device, wherein a steam channel is arranged at the periphery of a heater, the steam channel is arranged to annularly wind the whole heater, and a radiating fin is arranged inside the heater and connected with the steam channel; the outer side of the evaporator is surrounded with a heat-insulating layer, and the steam inlet is connected to the high-temperature steam outlet through a pipeline; a first branch pipe is arranged on the second connecting pipe, a battery valve is arranged on the first branch pipe, and the first branch pipe of the first-effect evaporator is connected to a feeding pipe of the second-effect heater through a first-effect discharging pipe; the top of the evaporator is provided with a third connecting pipe, and the third connecting pipe is provided with a high-temperature steam first air inlet connected with the double-effect heater through a branch pipe; this device is through the heating high temperature steam passageway from the new design heater to set up the conversion efficiency of fin in order to increase steam in the inside of heater, realize continuous feeding and ejection of compact through control, thereby improve continuous operation nature and promote production efficiency.
Description
Technical Field
The utility model relates to a pharmacy equipment technique, concretely relates to practical economic benefits and social benefits enrichment facility.
Background
The concentrator is used as the equipment of the concentration production process, and the concentrator has single effect, double effect, triple effect and multiple effect. Among them, the double effect concentrator is one of the most common forms. In the existing double-effect concentrator, a first-effect evaporation chamber and a second-effect heater are independently concentrated
And (4) condensing steam and the like generated in the first effect to enter the second effect again from the upper end of the heater of the second effect, directly discharging the steam into the evaporation chamber through the steam pipe at the top, and performing primary evaporation test. The steam that evaporates all is the most ordinary steam usually, and not contain the steam that the material needs the condensation, and these steam reentry two effects not only cause the redundancy of two effects, also are a waste simultaneously, and these steam of reasonable utilization is not had to, when concentrated completion is arranged material, the concentrated production efficiency of influence that accomplishes alone when arranging the material.
SUMMERY OF THE UTILITY MODEL
An object of the utility model is to provide a practical economic benefits and social benefits enrichment facility solves the wasting of resources of current economic benefits and social benefits concentrator, the low problem of production efficiency.
In order to solve the technical problem, the utility model adopts the following technical scheme:
a practical double-effect concentration device comprises a heater and an evaporator, wherein the heater and the evaporator are arranged into 2 groups, namely a first-effect evaporator, a second-effect evaporator, a first-effect heater and a second-effect heater; the upper part of the heater is provided with a first connecting pipe connected with the evaporator, the bottom of the evaporator is provided with a second connecting pipe connected to the bottom of the heater, and the bottom of the heater is provided with a feeding pipe; the periphery of the heater is provided with a steam channel, the steam channel is arranged to be wound around the whole heater in a ring shape, the upper end of the steam channel is provided with a first high-temperature steam inlet, the bottom of the steam channel is provided with a second high-temperature steam inlet, the middle of the steam channel is provided with a high-temperature steam outlet, a radiating fin is arranged in the heater and connected with the steam channel, and the bottom of the steam channel is provided with a; the outer side of the evaporator is surrounded with a heat-insulating layer, the bottom of the heat-insulating layer is provided with a steam inlet, the top of the heat-insulating layer is provided with a steam outlet, and the steam inlet is connected to the high-temperature steam outlet through a pipeline; a first branch pipe is arranged on the second connecting pipe, a battery valve is arranged on the first branch pipe, and the first branch pipe of the first-effect evaporator is connected to a feeding pipe of the second-effect heater through a first-effect discharging pipe; the top of the evaporator is provided with a third connecting pipe, the third connecting pipe of the first-effect evaporator is connected to the feeding pipe of the second-effect heater, and the third connecting pipe is provided with a high-temperature steam first air inlet connected to the second-effect heater through a branch pipe.
Furthermore, a solenoid valve is arranged on the third connecting pipe, the third connecting pipe is arranged at the upper end of the solenoid valve, and the solenoid valve is arranged on the branch pipe on the third connecting pipe.
Furthermore, a waste discharge pipe is arranged at the bottom of the heater, and an electromagnetic valve is arranged on the waste discharge pipe.
Furthermore, waste discharge pipes at the bottoms of the first-effect heater and the second-effect heater are connected through a comprehensive pipe, a circulating motor is arranged on the comprehensive pipe, a waste discharge branch pipe is arranged on the comprehensive pipe, and an electromagnetic valve is arranged on the waste discharge branch pipe.
Furthermore, a branch pipe is arranged on the waste discharge pipe and connected to the high-temperature steam outlet, and an electromagnetic valve is arranged on the branch pipe.
Furthermore, except the battery valves on the waste discharge pipe and the waste discharge pipe branch pipe, all the electromagnetic valves are set as one-way valves.
Compared with the prior art, the beneficial effects of the utility model are that:
this device is through the heating high temperature steam passageway from the newly-designed heater to set up the conversion efficiency of fin in order to increase steam in the inside of heater, simultaneously, carry out reuse to the remaining waste heat of steam, thereby improved the utilization ratio of energy and then reduced the waste of the energy, reach the purpose that energy-conservation reaches, and, realize continuous feeding and ejection of compact through the control of check valve non-return, thereby improve continuous operability and promote production efficiency.
Drawings
Fig. 1 is a schematic structural diagram of the present invention.
In the figure, 1-effect evaporator, 2-effect heater, 3 first connecting pipe, 4-second connecting pipe, 5-sampling port, 6-first branch pipe, 7-feeding pipe, 8-waste discharging pipe, 11-steam outlet, 12-condensed water outlet, 13-steam inlet, 14-third connecting pipe, 15-comprehensive connecting pipe, 16-effect discharging pipe, 17-waste discharging branch pipe, 21-high temperature steam first inlet, 22-high temperature steam second inlet, 23-high temperature steam outlet, 24-steam channel, 25-radiating fin, 26 condensed water outlet, 201-two-effect heater and 101-two-effect evaporator.
Detailed Description
In order to make the objects, technical solutions and advantages of the present invention more clearly understood, the present invention is further described in detail below with reference to the accompanying drawings and embodiments. It should be understood that the specific embodiments described herein are merely illustrative of the invention and are not intended to limit the invention.
Example 1:
the practical double-effect concentration device comprises a heater and an evaporator, wherein the heater and the evaporator are arranged into 2 groups, namely a first-effect evaporator 1, a second-effect evaporator 101, a first-effect heater 2 and a second-effect heater 201. In the setting, the unified equipment is used for one effect and two effects, specifically, a first connecting pipe 3 is arranged at the upper part of the heater and connected with the evaporator, a second connecting pipe 4 is arranged at the bottom of the evaporator and connected to the bottom of the heater, and a feeding pipe 7 is arranged at the bottom of the heater. In order to effectively utilize high-temperature steam, a steam channel 24 is arranged on the periphery of the heater, the steam channel 24 is arranged to be wound into a ring shape to form the whole heater, a first high-temperature steam inlet 21 is arranged at the upper end of the steam channel 24, a second high-temperature steam inlet 22 is arranged at the bottom of the steam channel, a high-temperature steam outlet 23 is arranged in the middle of the steam channel, the steam channel is heated through two sides and then is uniformly removed after being gathered in the middle of the steam channel, and materials inside the heater can be better. In order to improve the use efficiency of heat energy and increase the conversion efficiency, a radiating fin 25 is arranged inside the heater and connected with a steam channel 24, and a condensed water outlet is arranged at the bottom of the steam channel 24. Follow further, in order to utilize the preheating that contains in the surplus steam better, enclose in the evaporimeter outside and be equipped with the heat preservation, heat preservation bottom of the layer is provided with steam inlet 13, and the top is provided with steam outlet 11, and steam inlet 13 is through pipe connection to high temperature steam outlet 23, and the waste heat through high temperature steam comes to keep warm the evaporimeter, reduces the waste of energy. In use, in order to improve the concentration efficiency, a first branch pipe 6 is arranged on the second connecting pipe 4, a battery valve is arranged on the first branch pipe 6, the first branch pipe 6 of the first-effect evaporator 1 is connected to a feeding pipe 7 of the second-effect heater through a first-effect discharging pipe 16, and the first-effect concentrate after the first-effect concentration is guided into the second-effect heater again for the second-effect concentration. A third connecting pipe 14 is arranged at the top of the evaporator, the third connecting pipe 14 of the first-effect evaporator 1 is connected to the feeding pipe 7 of the second-effect heater, and a first high-temperature steam inlet 21 branched and connected to the second-effect heater 201 is arranged on the third connecting pipe 14. The effective components evaporated in the first effect are introduced into the second effect again for second effect concentration.
Example 2:
on the basis of the above embodiments, in this embodiment, the electromagnetic valve is disposed on the third connecting pipe 14, the third connecting pipe 14 is disposed at the upper end of the electromagnetic valve, and the electromagnetic valve is disposed on the branch pipe on the third connecting pipe 14, and the branch pipe is disposed above the electromagnetic valve, so that selective operation can be performed as required.
Example 3:
on the basis of the above embodiment, in this embodiment, the bottom of the heater is provided with a waste discharge pipe 8 for discharging waste, and the waste discharge pipe 8 is provided with an electromagnetic valve.
Example 4:
on the basis of the above embodiment, in this embodiment, the first-effect heater 2 and the waste discharge pipe 8 at the bottom of the second-effect heater 201 are connected through the comprehensive pipe 15, the circulation motor is arranged on the comprehensive pipe 15, the waste discharge branch pipe 17 is arranged on the comprehensive pipe 15, and the electromagnetic valve is arranged on the waste discharge branch pipe 17.
Example 5:
on the basis of the above embodiments, in this embodiment, the waste discharge pipe 8 is provided with a branch pipe connected to the high-temperature steam outlet 23, and the branch pipe is provided with an electromagnetic valve, so that external steam is used for back flushing when necessary, which is also convenient for control.
Example 6:
in addition to the above embodiments, in this embodiment, for the convenience of control and prevention of reverse flow, all the solenoid valves are provided as check valves except the battery valves in the waste discharge pipe 8 and the branch pipes of the waste discharge pipe 8.
Reference throughout this specification to "example 1", "example 2", "example 3", "example 4", and so forth, means that a particular feature, structure, or characteristic described in connection with the example is included in at least one embodiment described generally throughout this application. The appearances of the same phrase in various places in the specification are not necessarily all referring to the same embodiment. Further, when a particular feature, structure, or characteristic is described in connection with any embodiment, it is submitted that it is within the scope of the invention to effect such feature, structure, or characteristic in connection with other embodiments.
Although the invention has been described herein with reference to a number of illustrative embodiments thereof, it should be understood that numerous other modifications and embodiments can be devised by those skilled in the art that will fall within the spirit and scope of the principles of this invention. More specifically, various variations and modifications are possible in the component parts and/or arrangements of the subject combination arrangement within the scope of the disclosure, the drawings and the appended claims. In addition to variations and modifications in the component parts and/or arrangements, other uses will also be apparent to those skilled in the art.
Claims (6)
1. A practical double-effect concentration device comprises a heater and an evaporator, wherein the heater and the evaporator are arranged into 2 groups, namely a first-effect evaporator (1), a second-effect evaporator (101), a first-effect heater (2) and a second-effect heater (201); the method is characterized in that: the upper part of the heater is provided with a first connecting pipe (3) connected with the evaporator, the bottom of the evaporator is provided with a second connecting pipe (4) connected to the bottom of the heater, and the bottom of the heater is provided with a feeding pipe (7); the periphery of the heater is provided with a steam channel (24), the steam channel (24) is arranged to be wound on the whole heater in a ring shape, the upper end of the steam channel (24) is provided with a high-temperature steam first air inlet (21), the bottom of the steam channel is provided with a high-temperature steam second air inlet (22), the middle of the steam channel is provided with a high-temperature steam outlet (23), a radiating fin (25) arranged in the heater is connected with the steam channel (24), and the bottom of the steam channel (24) is provided with a; the outer side of the evaporator is surrounded with a heat insulation layer, the bottom of the heat insulation layer is provided with a steam inlet (13), the top of the heat insulation layer is provided with a steam outlet (11), and the steam inlet (13) is connected to a high-temperature steam outlet (23) through a pipeline; a first branch pipe (6) is arranged on the second connecting pipe (4), a battery valve is arranged on the first branch pipe (6), and the first branch pipe (6) of the first-effect evaporator (1) is connected to a feeding pipe (7) of the second-effect heater through a first-effect discharging pipe (16); the top of the evaporator is provided with a third connecting pipe (14), the third connecting pipe (14) of the first-effect evaporator (1) is connected to the feeding pipe (7) of the second-effect heater, and the third connecting pipe (14) is provided with a high-temperature steam first air inlet (21) which is connected to the second-effect heater (201) through a branch pipe.
2. The practical double effect concentrating device according to claim 1, wherein: an electromagnetic valve is arranged on the third connecting pipe (14), the third connecting pipe (14) is arranged at the upper end of the electromagnetic valve, and the electromagnetic valve is arranged on a branch pipe on the third connecting pipe (14).
3. The practical double effect concentrating device according to claim 1, wherein: the bottom of the heater is provided with a waste discharge pipe (8), and the waste discharge pipe (8) is provided with an electromagnetic valve.
4. The practical double effect concentrating device according to claim 1, wherein: the waste discharge pipe (8) at the bottom of the first-effect heater (2) and the second-effect heater (201) is connected through a comprehensive pipe (15), a circulating motor is arranged on the comprehensive pipe (15), a waste discharge branch pipe (17) is arranged on the comprehensive pipe (15), and an electromagnetic valve is arranged on the waste discharge branch pipe (17).
5. The practical double effect concentrating device according to claim 3, wherein: the waste discharge pipe (8) is provided with a branch pipe connected to the high-temperature steam outlet (23), and the branch pipe is provided with an electromagnetic valve.
6. The practical double effect concentrating device according to claim 1, wherein: except for the battery valves on the waste discharge pipe (8) and the branch pipe of the waste discharge pipe (8), all the electromagnetic valves are set as one-way valves.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201922311916.XU CN211383841U (en) | 2019-12-20 | 2019-12-20 | Practical economic benefits and social benefits enrichment facility |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201922311916.XU CN211383841U (en) | 2019-12-20 | 2019-12-20 | Practical economic benefits and social benefits enrichment facility |
Publications (1)
Publication Number | Publication Date |
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CN211383841U true CN211383841U (en) | 2020-09-01 |
Family
ID=72227658
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
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CN201922311916.XU Expired - Fee Related CN211383841U (en) | 2019-12-20 | 2019-12-20 | Practical economic benefits and social benefits enrichment facility |
Country Status (1)
Country | Link |
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CN (1) | CN211383841U (en) |
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2019
- 2019-12-20 CN CN201922311916.XU patent/CN211383841U/en not_active Expired - Fee Related
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CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20200901 |
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CF01 | Termination of patent right due to non-payment of annual fee |