CN209354320U - A kind of compressor heat energy utilization system - Google Patents
A kind of compressor heat energy utilization system Download PDFInfo
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- CN209354320U CN209354320U CN201822174202.4U CN201822174202U CN209354320U CN 209354320 U CN209354320 U CN 209354320U CN 201822174202 U CN201822174202 U CN 201822174202U CN 209354320 U CN209354320 U CN 209354320U
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- connecting pipeline
- compensator
- heat exchanger
- condenser
- circulating pump
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Abstract
The utility model discloses a kind of compressor heat energy utilization systems, including expander inlet separator, the expander inlet separator connects expanding machine, the expanding machine connects condenser, the condenser connects compensator, the compensator connects circulating pump, the circulating pump connects afterheat heat exchanger, the afterheat heat exchanger connects expander inlet separator, this compressor heat energy utilization system structure advantages of simple, novel ingenious, easy to operate practical, it both can be with energy-saving and emission-reduction, thermal energy is recycled, can also economize on resources, reduce cost.
Description
Technical field
The utility model relates to heat recovery technology fields, and in particular to a kind of compressor heat energy utilization system.
Background technique
In recent years, with the industrialized raising in China, various compressors are widely used, gas temperature after compressor compresses gas
Degree can be increased to 80 to 150 degree, send after gas is cooled to follow up device and use, the heat that gas contains does not obtain abundant benefit
With.
Utility model content
The purpose of this utility model is exactly to solve the above-mentioned problems, to provide a kind of compressor heat energy utilization system.
To achieve the goals above, the utility model adopts the following technical solution:
A kind of compressor heat energy utilization system, including cryogen level-one entrance, cryogen secondary inlet, unstripped gas level-one entrance,
Unstripped gas secondary inlet, unstripped gas three-level entrance, unstripped gas primary outlet, unstripped gas secondary exit port, unstripped gas three-level export, are cold
Agent primary outlet, cryogen secondary exit port, afterheat heat exchanger to expander inlet separator connecting pipeline, expander inlet separation
Device, expander inlet separator to expanding machine connecting pipeline, expanding machine, expanding machine to condenser connecting pipeline, condenser, condensation
Device is to compensator connecting pipeline, compensator, compensator to circulating pump connecting pipeline, intermediate medium, circulating pump, circulating pump to waste heat
Heat exchanger connecting pipeline, afterheat heat exchanger.
Be successively arranged at the top of the afterheat heat exchanger cryogen level-one entrance, cryogen secondary inlet, unstripped gas level-one entrance,
To expander inlet separator connecting pipeline, the waste heat is changed for unstripped gas secondary inlet, unstripped gas three-level entrance, afterheat heat exchanger
Hot device bottom is successively arranged cryogen primary outlet, cryogen secondary exit port, unstripped gas primary outlet, unstripped gas secondary exit port, raw material
The outlet of gas three-level, circulating pump to afterheat heat exchanger connecting pipeline, the afterheat heat exchanger are another to expander inlet connecting pipeline
One end is connected with expander inlet separator, is connected with expander inlet separator extremely at the top of the expander inlet separator
Expanding machine connecting pipeline, one end of expander inlet separator to the expanding machine connecting pipeline is connected with expanding machine, described swollen
The side of swollen machine is connected with expanding machine to condenser connecting pipeline, and the other end of the expanding machine to condenser connecting pipeline connects
There is condenser, the side of the condenser is connected with condenser to compensator connecting pipeline, and the condenser to compensator connects
The other end of pipeline is connected with compensator, and the side of the balance pipe is connected with compensator to circulating pump connecting pipeline, described flat
The other end of weighing apparatus tank to circulating pump connecting pipeline is connected with circulating pump, and the bottom of the circulating pump is equipped with intermediate medium, described to follow
The side of ring pump is connected with the circulating pump to afterheat heat exchanger connecting pipeline.
Further, the afterheat heat exchanger to expander inlet separator connecting pipeline, expander inlet separator extremely
Expanding machine connecting pipeline, expanding machine to condenser connecting pipeline, condenser to compensator connecting pipeline, compensator to circulating pump connect
There is screw thread at the both ends of adapter tube line and circulating pump to afterheat heat exchanger connecting pipeline (22), easy to disassemble, are conducive to daily dimension
Shield and cleaning.
The beneficial effects of the utility model are: structure is simple and convenient to operate, convenient for safeguarding, in system work, centre is situated between
Matter can be recycled, and effectively save resource, reduce production cost.
Detailed description of the invention
FIG. 1 is a schematic structural view of the utility model.
In figure: 1, cryogen level-one entrance, 2, cryogen secondary inlet, 3, unstripped gas level-one entrance, 4, unstripped gas secondary inlet,
5, unstripped gas three-level entrance, 6, unstripped gas primary outlet, 7, unstripped gas secondary exit port, 8, the outlet of unstripped gas three-level, 9, cryogen one
Grade outlet, 10, cryogen secondary exit port, 11, afterheat heat exchanger to expander inlet separator connecting pipeline, 12, expander inlet
Separator, 13, expander inlet separator to expanding machine connecting pipeline, 14, expanding machine, 15, expanding machine to condenser connecting tube
Line, 16, condenser, 17, condenser to compensator connecting pipeline, 18, compensator, 19, compensator to circulating pump connecting pipeline,
20, intermediate medium, 21, circulating pump, 22, circulating pump to afterheat heat exchanger connecting pipeline, 23, afterheat heat exchanger.
Specific embodiment
The following examples can make those skilled in the art that the utility model be more fully understood, but not in any way
Limit the utility model.
As shown in Figure 1, a kind of compressor heat energy utilization system, including cryogen level-one entrance 1, cryogen secondary inlet 2, raw material
Gas level-one entrance 3, unstripped gas secondary inlet 4, unstripped gas three-level entrance 5, unstripped gas primary outlet 6, unstripped gas secondary exit port 7,
Unstripped gas three-level outlet 8, cryogen primary outlet 9, cryogen secondary exit port 10, afterheat heat exchanger to expander inlet separator connect
Pipeline 11, expander inlet separator 12, expander inlet separator to expanding machine connecting pipeline 13, expanding machine 14, expanding machine
To condenser connecting pipeline 15, condenser 16, condenser to compensator connecting pipeline 17, compensator 18, compensator to circulating pump
Connecting pipeline 19, intermediate medium 20, circulating pump 21, circulating pump to afterheat heat exchanger connecting pipeline 22, afterheat heat exchanger 23.
The top of the afterheat heat exchanger 23 is successively arranged cryogen level-one entrance 1, cryogen secondary inlet 2, unstripped gas level-one
Entrance 3, unstripped gas secondary inlet 4, unstripped gas three-level entrance 5, afterheat heat exchanger to expander inlet separator connecting pipeline 11,
23 bottom of afterheat heat exchanger is successively arranged cryogen primary outlet 9, cryogen secondary exit port 10, unstripped gas primary outlet 6, raw material
Gas secondary exit port 7, unstripped gas three-level export 8, circulating pump to afterheat heat exchanger connecting pipeline 22, the afterheat heat exchanger to expansion
The other end of machine entrance connecting pipeline 11 is connected with expander inlet separator 12, the top of the expander inlet separator 12
Expander inlet separator is connected with to expanding machine connecting pipeline (13), the expander inlet separator to expanding machine connecting tube
One end of line 13 is connected with expanding machine 14, and the side of the expanding machine 14 is connected with expanding machine to condenser connecting pipeline 15, institute
The other end for stating expanding machine to condenser connecting pipeline 15 is connected with condenser 16, and the side of the condenser 16 is connected with condensation
For device to compensator connecting pipeline 17, the other end of the condenser to compensator connecting pipeline 10 is connected with compensator 18, described
The side of balance pipe 18 is connected with compensator to circulating pump connecting pipeline 19, and the compensator is another to circulating pump connecting pipeline 19
One end is connected with circulating pump 21, and the bottom of the circulating pump 21 is equipped with intermediate medium 20, and the side of the circulating pump 21 is connected with
The circulating pump is to afterheat heat exchanger connecting pipeline 22.
In this preferred embodiment, the afterheat heat exchanger to expander inlet separator connecting pipeline 11, expander inlet
Separator is to expanding machine connecting pipeline 13, expanding machine to condenser connecting pipeline 15, condenser to compensator connecting pipeline 17, flat
There is screw thread at the both ends of weighing apparatus tank to circulating pump connecting pipeline 19 and circulating pump to afterheat heat exchanger connecting pipeline 22.
The utility model principle is as follows: can be divided into two flow paths, i.e. processing medium flow path and intermediate Jie when the system works
Mass flow road, processing medium flow path, that is, cryogen level-one entrance 1, the azeotrope of cryogen secondary inlet 2 and unstripped gas level-one entrance 3,
The unstripped gas of unstripped gas secondary inlet 4, unstripped gas three-level entrance 5, five road gases under respective pressure, temperature, flow all into
Enter afterheat heat exchanger (23) and carry out heat exchange, after temperature fades to 59.7 DEG C, respectively by cryogen primary outlet 9, cryogen second level
Outlet 10, unstripped gas primary outlet 6, unstripped gas secondary exit port 7, unstripped gas three-level outlet 8 return to original respective cooler
In continue to cool down.
Intermediate medium 20 is used to absorb waste heat, and intermediate medium is pressurized to 2.6MPa from compensator 18 into circulating pump 21, then
Heat is absorbed in afterheat heat exchanger 23 and is vaporized, and is superheated to 110 DEG C, and isolating in expander inlet separator 12 may deposit
Liquid after, the expanding end into expanding machine 14 is expanded and output work, the power generation of the function driven generator of output.From expansion
The pressure for the intermediate medium 20 that the expanding end of generating set comes out is 1.4MPa, temperature is 65 DEG C, into cold in condenser 16
But water takes away heat intermediate medium 20 is made to be cooled to 38 DEG C and be condensed into subcooled liquid, the liquid back in compensator 18,
Intermediate medium is so recycled, and can economize on resources, and reduces production cost.
It will be understood by those skilled in the art that above embodiments are only exemplary embodiments, without departing substantially from the utility model
In the case where spirit and scope, a variety of variations can be carried out, replaced and changed.
Claims (2)
1. a kind of compressor heat energy utilization system, which is characterized in that including cryogen level-one entrance (1), cryogen secondary inlet (2),
Unstripped gas level-one entrance (3), unstripped gas secondary inlet (4), unstripped gas three-level entrance (5), unstripped gas primary outlet (6), raw material
Gas secondary exit port (7), unstripped gas three-level outlet (8), cryogen primary outlet (9), cryogen secondary exit port (10), afterheat heat exchanger are extremely
Expander inlet separator connecting pipeline (11), expander inlet separator (12), expander inlet separator to expanding machine connect
Adapter tube line (13), expanding machine (14), expanding machine to condenser connecting pipeline (15), condenser (16), condenser to compensator connect
Adapter tube line (17), compensator (18), compensator to circulating pump connecting pipeline (19), intermediate medium (20), circulating pump (21), circulation
It pumps to afterheat heat exchanger connecting pipeline (22), afterheat heat exchanger (23)；
Cryogen level-one entrance (1), cryogen secondary inlet (2), unstripped gas one are successively arranged at the top of the afterheat heat exchanger (23)
Grade entrance (3), unstripped gas secondary inlet (4), unstripped gas three-level entrance (5), afterheat heat exchanger to expander inlet separator connect
Adapter tube line (11), afterheat heat exchanger (23) bottom are successively arranged cryogen primary outlet (9), cryogen secondary exit port (10), original
Expect that gas primary outlet (6), unstripped gas secondary exit port (7), unstripped gas three-level export (8), circulating pump to afterheat heat exchanger connecting tube
The other end of line (22), the afterheat heat exchanger to expander inlet connecting pipeline (11) is connected with expander inlet separator
(12), expander inlet separator is connected with to expanding machine connecting pipeline at the top of the expander inlet separator (12)
(13), one end of the expander inlet separator to expanding machine connecting pipeline (13) is connected with expanding machine (14), the expansion
The side of machine (14) is connected with expanding machine to condenser connecting pipeline (15), the expanding machine to condenser connecting pipeline (15)
The other end is connected with condenser (16), and the side of the condenser (16) is connected with condenser to compensator connecting pipeline (17),
The other end of the condenser to compensator connecting pipeline (17) is connected with compensator (18), and the side of the compensator (18) connects
Compensator is connected to circulating pump connecting pipeline (19), the other end of the compensator to circulating pump connecting pipeline (19), which is connected with, to follow
Ring pumps (21), and the bottom of the circulating pump (21) is equipped with intermediate medium (20), and the side of the circulating pump (21) is connected with described
Circulating pump is to afterheat heat exchanger connecting pipeline (22).
2. a kind of compressor heat energy utilization system according to claim 1, which is characterized in that the afterheat heat exchanger is to swollen
Swollen machine entrance separator connecting pipeline (11), expander inlet separator to expanding machine connecting pipeline (13), expanding machine to condensation
Device connecting pipeline (15), condenser to compensator connecting pipeline (17), compensator to circulating pump connecting pipeline (19) and circulating pump
There is screw thread to the both ends of afterheat heat exchanger connecting pipeline (22).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201822174202.4U CN209354320U (en) | 2018-12-24 | 2018-12-24 | A kind of compressor heat energy utilization system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201822174202.4U CN209354320U (en) | 2018-12-24 | 2018-12-24 | A kind of compressor heat energy utilization system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN209354320U true CN209354320U (en) | 2019-09-06 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201822174202.4U Active CN209354320U (en) | 2018-12-24 | 2018-12-24 | A kind of compressor heat energy utilization system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN209354320U (en) |
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2018
- 2018-12-24 CN CN201822174202.4U patent/CN209354320U/en active Active
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