Overall structure system of acetone vapor compressor
By combining a dry gas seal and an inlet flow meter with an anti-surge valve, the problems of easy seal wear and insufficient flow in conventional steam compressors are solved. This achieves effective sealing and increased flow for acetone media, simplifies the structure, and improves detection accuracy and service life.
Patent Information
- Application Number
- CN202423084625.9
- Authority / Receiving Office
- CN · China
- Patent Type
- Utility models(China)
- Current Assignee / Owner
- Filing Date
- 2024-12-13
- Publication Date
- 2025-11-07
- Estimated Expiration
- 2034-12-13
AI Technical Summary
In existing technologies, the carbon ring seals of conventional steam compressors are prone to wear and cannot be used for toxic, flammable and explosive acetone media. Screw steam compressors have small flow rates, and multi-stage centrifugal compressors have complex structures and high costs.
By adopting dry gas sealing technology, combined with an imported flow meter and anti-surge valve, the structure is simplified, the sealing effect and service life are improved, the working flow is increased, and the structure of the multi-stage centrifugal compressor is simplified.
It achieves effective sealing of toxic, flammable and explosive media, extends service life, improves flow rate and structural simplicity, and enhances the accuracy of surge condition detection.
Smart Images
Figure CN223524007U_ABST
Abstract
Description
TECHNICAL FIELD
[0001] The utility model belongs to compressor technical field especially relates to a whole structure system of acetone steam compressor. BACKGROUND
[0002] The existing conventional single-stage centrifugal steam compressor in domestic is usually used for re-compression of water vapor medium, and temperature and pressure are improved. The conventional water vapor single-stage centrifugal compressor adopts carbon ring seal, and the carbon ring seal is easy to wear, and is not suitable for the scene with high sealing requirement of toxic, flammable and explosive medium such as acetone. The steam compressor for organic medium has a screw steam compressor and a centrifugal multi-stage compressor, the screw steam compressor has small flow, and cannot meet the demand of large flow; the centrifugal multi-stage compressor has complex structure and complex control logic, and has high cost. CONTENT OF UTILITY MODEL
[0003] The utility model discloses a kind of whole structure systems of acetone steam compressor, the dry gas seal technology used makes that compressor shaft end leakage is lower, service life is longer, more suitable for the occasion of toxic harmful, flammable and explosive organic steam.
[0004] In order to achieve the above purpose, the technical scheme of the utility model is as follows: a kind of whole structure system of acetone steam compressor, including driving motor, steam compressor head, outlet assembly and import component, the steam compressor head includes volute, gas inlet shell, rotor, dry gas seal and gear box;The gas inlet shell is located at the gas inlet end of volute, and the driving motor is connected with the gear box;The output shaft of the gear box is connected with the rotor after passing through the connecting hole on the volute, and is used to drive the rotation of the rotor, and the output shaft is provided with dry gas seal between the connecting hole;The import component is connected with the gas inlet shell, and the outlet assembly is connected with the outlet of the volute.
[0005] Further, the import component includes import pipe, import taper pipe, import expansion joint and import flowmeter;The small diameter end of the import taper pipe is connected with the gas inlet shell, and the large diameter end of the import taper pipe and import pipe are connected with the two sides of import expansion joint respectively;The import flowmeter is installed on import pipe.
[0006] Further, the outlet assembly includes outlet pipe, outlet taper pipe and outlet expansion joint, the small diameter end of the outlet taper pipe is connected with the outlet of volute, and the large diameter end of the outlet taper pipe and outlet pipe are connected with the two sides of outlet expansion joint respectively.
[0007] Further, the outlet pipe is connected with anti-surge pipe, and the anti-surge valve is connected on the anti-surge pipe.
[0008] Further, the outlet pipe is connected with cooling system.
[0009] The beneficial effects of the technical solution are that the air inlet shell guides the gas into the rotor, the gear box increases the input rotating speed of the driving motor, the driving rotor works, and finally the gas enters the volute to slow down and expand the pressure.
[0010] The acetone steam compressor of the technical solution is different from the conventional water vapor compressor in sealing, the conventional water vapor compressor usually adopts carbon ring sealing, the carbon ring sealing is easy to wear, and is not suitable for scenes with high sealing requirements for toxic, flammable and explosive media such as acetone, and the sealing effect and service life of the dry gas sealing of the technical solution are better than those of the carbon ring sealing. In addition, the anti-surge control of the water vapor compressor in the industry basically adopts motor current and power fluctuation to realize surge detection. The combination of the inlet flow meter and the anti-surge valve of the technical solution is more direct and accurate for detecting the surge condition. Compared with the screw steam compressor, the acetone steam compressor of the technical solution is a single-stage centrifugal steam compressor, and the working flow is larger. Compared with the multi-stage centrifugal compressor, the head structure of the acetone steam compressor of the technical solution is simpler. BRIEF DESCRIPTION OF DRAWINGS
[0011] Figure 1 It is a structure schematic view of the whole structure system of the acetone steam compressor.
[0012] Figure 2 It is a structure schematic view of the steam compressor head. DETAILED DESCRIPTION
[0013] The following will be further described in detail through specific embodiments:
[0014] The reference signs in the drawings of the specification include: driving motor 1, integrated oil system base 2, steam compressor head 3, volute 4, outlet cone pipe 5, outlet expansion joint 6, outlet pipe 7, cooling system 8, anti-surge pipe 9, anti-surge valve 10, inlet cone pipe 11, inlet expansion joint 12, inlet pipe 13, gear box 14, air inlet shell 15, rotor 16, dry gas sealing 17, inlet flow meter 18.
[0015] The technical solutions in the embodiments of the utility model will be clearly and completely described below with reference to the drawings in the embodiments of the utility model. Obviously, the described embodiments are only part of the embodiments of the utility model, rather than all the embodiments. Based on the embodiments of the utility model, all other embodiments obtained by those skilled in the art without creative labor belong to the protection scope of the utility model.
[0016] The embodiments are basically as shown in the accompanying drawings: Figures 1-2 An overall structure system of an acetone vapor compressor comprises an integrated oil system base 2, a driving motor 1, a vapor compressor head 3, an outlet assembly and an inlet assembly. The integrated oil system base 2 provides lubrication for the vapor compressor head 3 and supports the driving motor 1, the vapor compressor head 3 and other components. Figure 2 As shown in the drawings, the vapor compressor head 3 comprises a volute 4, an inlet casing 15, a rotor 16, a dry gas seal 17 and a gear box 14. The inlet casing 15 is located at the gas inlet end of the volute 4, and the driving motor 1 is connected with the gear box 14. The output shaft of the gear box 14 is connected with the rotor 16 after penetrating through the connecting hole on the volute 4 and is used to drive the rotor 16 to rotate. The dry gas seal 17 is arranged between the output shaft and the connecting hole. The inlet assembly is connected with the inlet casing 15, and the outlet assembly is connected with the outlet of the volute 4.
[0017] The inlet assembly comprises an inlet pipe 13, an inlet taper pipe 11, an inlet expansion joint 12 and an inlet flowmeter 18. The small-diameter end of the inlet taper pipe 11 is connected with the inlet casing 15, and the large-diameter end of the inlet taper pipe 11 and the inlet pipe 13 are respectively connected with the two sides of the inlet expansion joint 12. The inlet flowmeter 18 is installed on the inlet pipe 13. The outlet assembly comprises an outlet pipe 7, an outlet taper pipe 5 and an outlet expansion joint 6. The small-diameter end of the outlet taper pipe 5 is connected with the outlet of the volute 4, the large-diameter end of the outlet taper pipe 5 and the outlet pipe 7 are respectively connected with the two sides of the outlet expansion joint 6. The anti-surge pipe 9 is connected with the outlet pipe 7, the anti-surge valve 10 is connected with the anti-surge pipe 9, and the cooling system 8 is connected with the outlet pipe 7.
[0018] The inlet casing 15 guides the gas into the rotor 16. The driving motor 1 is accelerated in speed by the gear box 14, and the rotor 16 is driven to work. Finally, the gas enters the volute 4 to be decelerated and expanded. The cooling system 8 cools the overheated steam at the outlet of the compressor to the saturated state to improve the steam heat exchange efficiency. The anti-surge valve 10 cooperates with the inlet flowmeter 18 to control the running state of the compressor. When the inlet flow of the compressor approaches the surge condition, the anti-surge valve 10 is opened to increase the inlet volume flow, so that the compressor is separated from the surge condition. The inlet taper pipe 11 and the outlet taper pipe 5 can control the steam flow rate. The inlet expansion joint 12 and the outlet expansion joint 6 can effectively prevent the problem of pipeline leakage caused by thermal deformation at the pipeline connection.
[0019] The acetone vapor compressor of the technical solution is different from the conventional water vapor compressor in sealing. The conventional water vapor compressor usually adopts carbon ring sealing. The carbon ring sealing is easy to wear and tear, and is not suitable for the scene of sealing toxic, flammable and explosive medium such as acetone. The sealing effect and service life of the dry gas seal 17 of the technical solution are superior to those of the carbon ring sealing. In addition, the anti-surge control of the water vapor compressor in the industry basically adopts motor current and power fluctuation to realize surge detection. The combination of the import flow meter 18 and the anti-surge valve 10 of the technical solution is more direct and accurate for detecting the surge condition. Compared with the screw type vapor compressor, the acetone vapor compressor of the technical solution is a single-stage centrifugal vapor compressor, and the working flow is larger. Compared with the multi-stage centrifugal compressor, the structure of the head 3 of the acetone vapor compressor of the technical solution is simpler.
[0020] It should be noted that in this document, the terms such as first and second are used only to distinguish one entity or operation from another, and do not necessarily require or imply any such actual relationship or order between such entities or operations. Moreover, the terms "include", "contain" or any other variants thereof are intended to cover non-exclusive inclusion, so that the process, method, article or equipment including a series of elements not only includes those elements, but also includes other elements not explicitly listed or inherent to such process, method, article or equipment.
[0021] The above is only an embodiment of the present application, and the common knowledge of specific structures and properties in the scheme is not described in detail. The ordinary skilled person in the art knows all the ordinary technical knowledge in the technical field of the application before the application date or the priority date, can know all the prior art in the field, and has the ability to apply conventional experimental means before that date. The ordinary skilled person in the art can improve and implement the present scheme based on their own ability under the guidance of the present application. Some typical known structures or known methods should not be an obstacle for the ordinary skilled person in the art to implement the present application. It should be noted that for those skilled in the art, without departing from the structure of the present application, a number of modifications and improvements can be made, which should be considered as the protection scope of the present application. These will not affect the effect and practicality of the present application. The protection scope of the present application should be subject to the content of its claims, and the specific implementation mode in the specification can be used to explain the content of the claims.
Claims
1. An overall structure system of an acetone vapor compressor characterized by: The application relates to a steam compressor, which comprises a driving motor (1), a steam compressor head (3), an outlet assembly and an inlet assembly, wherein the steam compressor head (3) comprises a volute (4), an air inlet casing (15), a rotor (16), a dry gas seal (17) and a gear box (14); the air inlet casing (15) is arranged at an air inlet end of the volute (4); the driving motor (1) is connected with the gear box (14); an output shaft of the gear box (14) is connected with the rotor (16) after penetrating through a connecting hole on the volute (4) and is used for driving the rotor (16) to rotate; the dry gas seal (17) is arranged between the output shaft and the connecting hole; the inlet assembly is connected with the air inlet casing (15); and the outlet assembly is connected with an outlet of the volute (4).
2. An overall structure system of an acetone vapor compressor according to claim 1, characterized in that: The inlet assembly comprises an inlet pipe (13), an inlet taper pipe (11), an inlet expansion joint (12) and an inlet flowmeter (18); the small-diameter end of the inlet taper pipe (11) is connected with the air inlet casing (15); the large-diameter end of the inlet taper pipe (11) and the inlet pipe (13) are respectively connected with two sides of the inlet expansion joint (12); and the inlet flowmeter (18) is arranged on the inlet pipe (13).
3. An integrated system of an acetone vapor compressor according to claim 2, characterized in that: The outlet assembly comprises an outlet pipe (7), an outlet taper pipe (5) and an outlet expansion joint (6); the small-diameter end of the outlet taper pipe (5) is connected with the outlet of the volute (4); the large-diameter end of the outlet taper pipe (5) and the outlet pipe (7) are respectively connected with two sides of the outlet expansion joint (6).
4. An integrated system of an acetone vapor compressor according to claim 3, characterized in that: The outlet pipe (7) is connected with an anti-surge pipe (9), and the anti-surge pipe (9) is connected with an anti-surge valve (10).
5. An integrated system of an acetone vapor compressor according to claim 3, characterized in that: The outlet pipe (7) is connected with a cooling system (8).