Silicon carbide steam jet vacuum pump
Technical Field
The invention relates to the technical field of steam jet vacuum pumps, in particular to a silicon carbide steam jet vacuum pump.
Background
The steam jet vacuum pump is a reliable and economical device for preparing vacuum by using steam as power, does not need electric power, does not have moving and rotating parts, has simple system and reliable operation, and is widely used. A common steam injector consists of four components, a steam chamber, a nozzle, a mixing chamber and a diffuser.
The common materials of the existing steam jet vacuum pump are carbon steel, cast iron and stainless steel, but other materials such as Monel alloy, hastelloy, polytetrafluoroethylene, carbon steel lining graphite and the like are also frequently adopted due to the application universality of the steam jet vacuum pump. But the selection of current material is used and can not satisfy the operating mode of high strength, high temperature, strong corruption simultaneously, especially when being taken out when containing strong corruption gas such as high temperature hydrofluoric acid in the container, the steam injector of current material can not satisfy the requirement of long-time steady operation, exists deformation, corruption, the risk of damage at any time, and the structure of current steam injection vacuum pump is complicated, and the equipment is inconvenient.
Disclosure of Invention
In order to overcome the defects of the technology, the invention aims to provide the silicon carbide steam jet vacuum pump.
The technical scheme includes that the silicon carbide steam jet vacuum pump comprises a silicon carbide nozzle for jetting steam, a steel lining tetrafluoro mixing chamber shell, a steel lining tetrafluoro diffuser and a metal pressing plate flange, wherein the steel lining tetrafluoro diffuser comprises a first conical tube, a cylindrical tube and a second conical tube, the first conical tube, the cylindrical tube and the second conical tube are coaxially arranged, two ends of the cylindrical tube are fixedly communicated with the small diameter end of the first conical tube and the small diameter end of the second conical tube respectively, two ends of the steel lining tetrafluoro mixing chamber shell are respectively provided with an inlet and an outlet, the inlet end of the steel lining tetrafluoro mixing chamber shell is fixedly provided with a first flange matched with the metal pressing plate flange, the outlet end of the steel lining tetrafluoro mixing chamber shell is fixedly communicated with the large diameter end of the first conical tube, the steel lining tetrafluoro mixing chamber shell is provided with a driven inlet for enabling mixed gas to enter the steel lining tetrafluoro mixing chamber shell, the silicon carbide nozzle is sequentially provided with a small diameter end of the first conical tube and the small diameter end of the second conical tube, two ends of the cylindrical tube are sequentially communicated with the cylindrical throat and the cylindrical expansion cavity, the cylindrical expansion cavity is formed by the cylindrical expansion cavity is communicated with the small diameter of the cylindrical expansion cavity, and the cylindrical expansion cavity is communicated with the cylindrical expansion cavity, and the diameter of the cylindrical expansion cavity is communicated with the expansion cavity, and the expansion cavity is communicated with the expansion cavity.
Further, the diameter of the large diameter end of the conical shrinkage cavity is larger than that of the large diameter end of the conical expansion cavity, and the inner diameter of the large diameter end of the first conical pipe is smaller than that of the large diameter end of the second conical pipe.
Further, the cylindrical steam cavity, the conical shrinkage cavity, the cylindrical throat cavity, the conical expansion cavity, the first conical pipe, the cylindrical pipe and the second conical pipe are coaxially arranged.
Compared with the prior art, the invention has the following beneficial effects:
The silicon carbide nozzle has the advantages of high strength, high heat conduction and high temperature resistance, continuous flushing of working steam can not influence the structure of the silicon carbide nozzle, stable operation of the steam ejector is guaranteed, the silicon carbide nozzle integrates two functions of a steam cavity and a nozzle, the structure of a steam ejector vacuum pump is simpler, assembly is more convenient, the steel lining tetrafluoro mixing chamber shell and the steel lining tetrafluoro diffuser adopt steel lining tetrafluoro materials due to complex forming technology of silicon carbide special-shaped parts, corrosion resistance requirements can be met, equipment investment can be correspondingly reduced, popularization and application of the silicon carbide steam ejector vacuum pump are facilitated, the corrosion resistance of a part of the silicon carbide steam ejector vacuum pump can be excellent, vacuumizing requirements under high temperature and strong corrosion conditions can be met, the blank of the application field of vacuum equipment is filled, the sealing surface of the silicon carbide nozzle is connected with the flange of the steel lining tetrafluoro mixing chamber shell through a flange in a flange butt clamping mode through a metal pressing plate flange, and the assembly reliability is improved.
Drawings
FIG. 1 is a schematic diagram of the structure of the present invention;
FIG. 2 is a schematic structural view of a silicon carbide nozzle of the present invention.
Detailed Description
The invention will now be described in detail with reference to the drawings and to specific embodiments.
As shown in fig. 1 to 2, the silicon carbide vapor injection vacuum pump comprises a silicon carbide nozzle 1 for injecting vapor, a steel-lined tetrafluoro mixing chamber shell 2, a steel-lined tetrafluoro diffuser 3 and a metal pressing plate flange 4, wherein the steel-lined tetrafluoro diffuser 3 comprises a first conical tube 301, a cylindrical tube 302 and a second conical tube 303, the first conical tube 301, the cylindrical tube 302 and the second conical tube 303 are coaxially arranged, two ends of the cylindrical tube 302 are fixedly communicated with the small diameter end of the first conical tube 301 and the small diameter end of the second conical tube 303 respectively, two ends of the steel-lined tetrafluoro mixing chamber shell 2 are provided with an inlet and an outlet respectively, the inlet end of the steel-lined tetrafluoro mixing chamber shell 2 is fixedly provided with a first flange 201 for being matched with the metal pressing plate flange 4, the outlet end of the steel-lined tetrafluoro mixing chamber shell 2 is fixedly communicated with the large diameter end of the first conical tube 301, the steel-lined tetrafluoro mixing chamber shell 2 is provided with an inlet 5 for allowing mixed gas to enter the steel-lined tetrafluoro mixing chamber shell 2, the silicon carbide nozzle 1 is sequentially connected with the cylindrical nozzle 1 along the direction of the cylindrical nozzle 1, the cylindrical silicon carbide chamber 1 is sequentially connected with the cylindrical silicon carbide chamber 101 and the other end of the cylindrical silicon carbide mixing chamber 1 by the cylindrical flange 1, and the cylindrical silicon carbide chamber 2 is sequentially connected with the cylindrical silicon carbide chamber 101 is sequentially communicated with the cylindrical silicon carbide chamber 1 by the cylindrical nozzle 1 through the cylindrical inlet and the cylindrical inlet end 101 and the cylindrical silicon carbide chamber 2 and the silicon carbide chamber 2 is sequentially provided with the silicon carbide chamber; the cylindrical steam chamber 101, the conical contraction chamber 102, the cylindrical throat chamber 103 and the conical expansion chamber 104 are all coaxially arranged, the two ends of the cylindrical throat cavity 103 are fixedly communicated with the small diameter end of the conical shrinkage cavity 102 and the small diameter end of the conical expansion cavity 104 respectively, and the large diameter end of the conical shrinkage cavity 102 is communicated with the cylindrical steam cavity 101.
The diameter of the large diameter end of the conical contraction cavity 102 is larger than that of the large diameter end of the conical expansion cavity 104, and the inner diameter of the large diameter end of the first conical tube 301 is smaller than that of the large diameter end of the second conical tube 303.
The cylindrical steam chamber 101, the conical shrink chamber 102, the cylindrical throat chamber 103, the conical expansion chamber 104, the first conical tube 301, the cylindrical tube 302 and the second conical tube 303 are coaxially arranged.
The steel lined tetrafluoro mixing chamber housing 2, the first conical tube 301, the cylindrical tube 302 and the second conical tube 303 are all made of steel lined tetrafluoro. The silicon carbide nozzle 1 is made of silicon carbide material.
The invention has excellent corrosion resistance at the contact part with the gas to be mixed, the flow rate of the working steam is increased after the working steam enters the silicon carbide nozzle 1 and is contracted by the conical contraction cavity 102, the Laval effect is generated when the working steam with the increased flow rate passes through the cylindrical throat cavity 103, the depressurization energy is completely converted into kinetic energy, the flow rate of the working steam reaches the sonic velocity, and the working steam is sprayed out from the large diameter end of the conical expansion cavity 104 to form vacuum, the gas to be mixed enters the steel-lined tetrafluoro mixing chamber shell 2 from the pumped inlet 5 under the action of pressure difference, enters the steel-lined tetrafluoro diffuser 3 after being mixed with the working steam, then the mixed gas passes through the steel-lined tetrafluoro diffuser 3 at the subsonic velocity, the flow rate of the mixed gas is reduced, the pressure is increased, and finally the mixed gas is discharged from the large diameter end of the second conical pipe 303.
The steel lined tetrafluoro mixing chamber housing 2 and the steel lined tetrafluoro diffuser 3 can be made in a variety of fluorine lined modes including tetrafluoro molding, PFA spraying, tetrafluoro winding, etc., and can be regarded as alternative fluorine lined modes as long as the manufacturing process can meet the design requirements.
According to different corrosion performances of the vacuumized medium, the silicon carbide nozzle 1 can be made of pressureless sintered silicon carbide or reaction sintered silicon carbide.
The steel lined tetrafluoro mixing chamber housing 2 and the steel lined tetrafluoro diffuser 3 can also be designed and fabricated using steel lined silicon carbide tubing technology, regardless of manufacturing costs.
The silicon carbide nozzle 1 can also be designed to be directly connected with the steel lined tetrafluoro mixing chamber shell 2 by a flange, but the flange holes on the silicon carbide flange plate can cause the cracking of the silicon carbide flange plate due to uneven stress of a fastener during locking, and the unreliable design is not taken as a preferable scheme.
The above examples give detailed embodiments and specific operation procedures on the premise of the technical solution of the present invention, but the scope of protection of the present invention is not limited to the above examples.