CN111359313B - Turbine vacuum system and steam-water separator thereof - Google Patents
Turbine vacuum system and steam-water separator thereof Download PDFInfo
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- CN111359313B CN111359313B CN202010464851.7A CN202010464851A CN111359313B CN 111359313 B CN111359313 B CN 111359313B CN 202010464851 A CN202010464851 A CN 202010464851A CN 111359313 B CN111359313 B CN 111359313B
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- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims abstract description 82
- 239000000706 filtrate Substances 0.000 claims abstract description 16
- 239000007788 liquid Substances 0.000 abstract description 25
- 238000000926 separation method Methods 0.000 abstract description 17
- 230000002349 favourable effect Effects 0.000 abstract description 2
- 238000000034 method Methods 0.000 description 11
- 238000004140 cleaning Methods 0.000 description 5
- 230000018044 dehydration Effects 0.000 description 4
- 238000006297 dehydration reaction Methods 0.000 description 4
- 238000010586 diagram Methods 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- 230000005484 gravity Effects 0.000 description 3
- 238000001514 detection method Methods 0.000 description 2
- 238000003780 insertion Methods 0.000 description 2
- 230000037431 insertion Effects 0.000 description 2
- 238000012423 maintenance Methods 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 238000009826 distribution Methods 0.000 description 1
- 230000003116 impacting effect Effects 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000002787 reinforcement Effects 0.000 description 1
- 230000000630 rising effect Effects 0.000 description 1
- 238000009991 scouring Methods 0.000 description 1
- 239000010865 sewage Substances 0.000 description 1
- 238000006467 substitution reaction Methods 0.000 description 1
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D45/00—Separating dispersed particles from gases or vapours by gravity, inertia, or centrifugal forces
- B01D45/04—Separating dispersed particles from gases or vapours by gravity, inertia, or centrifugal forces by utilising inertia
- B01D45/08—Separating dispersed particles from gases or vapours by gravity, inertia, or centrifugal forces by utilising inertia by impingement against baffle separators
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- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Separating Particles In Gases By Inertia (AREA)
Abstract
The invention provides a turbine vacuum system and a steam-water separator thereof, wherein the steam-water separator comprises a cylinder, a filtrate pump, a vertical baffle plate sleeved in the cylinder and an inclined baffle plate positioned at the bottom of the vertical baffle plate, wherein the side wall of the cylinder is provided with an air inlet, and the top of the cylinder is provided with an air outlet; the bottom of the barrel is provided with a water outlet, the filtrate pump is communicated with the water outlet, and the inclined direction of the inclined baffle plate faces the water outlet; at least one of the inner wall of the cylinder body, the inner wall and the outer wall of the vertical baffle is provided with a plurality of V-shaped flow deflectors, and the opening direction of the V-shaped flow deflectors is consistent with the flow direction of the air flow in the cylinder body. The steam-water separator utilizes the annular vertical baffle and the V-shaped flow deflectors distributed on the inner wall of the cylinder body to guide and divide air flow, so that steam-water separation is fully realized, the separation efficiency is high, the energy loss is small, the inclined baffle at the bottom of the cylinder body is favorable for thorough liquid drainage, and the steam-water separator is suitable for being used in a turbine vacuum system.
Description
Technical Field
The invention relates to the technical field of vacuum dehydration, in particular to a turbine vacuum system and a steam-water separator thereof.
Background
The existing steam-water separator applied to the papermaking vacuum dehydration process mainly comprises a cyclone type steam-water separator, a baffle type steam-water separator and a gravity type steam-water separator. The air inlet of the cyclone-type steam-water separator is positioned on the side surface of the cylinder wall, airflow rotates along the cylinder wall after entering the cyclone-type steam-water separator, and steam-water separation is realized by means of centrifugal force. The principle of the baffle type steam-water separator is that gas entering the device is guided to pass through a set baffle region, so that the gas flow continuously collides with the baffle to realize steam-water separation. The baffle guides the gas to the bottom of the cylinder body, and the gas flow impact is large due to the adoption of right-angle steering; the area is small as a steam-water buffer area, so that part of gas is mixed in liquid and is discharged by the filtrate pump, and meanwhile, the liquid containing air bubbles can cause the cavitation phenomenon of the pump when being discharged by the filtrate pump, so that the service life of the filtrate pump is shortened. In the process of forming rotational flow, the cyclone-type steam-water separator and the baffle-type steam-water separator have large energy loss, so that the load of the vacuum pump is increased, and the efficiency is reduced.
The principle of the gravity type steam-water separator is that the gravity of gas and floating liquid drops is different to generate a settling effect, the steam-water separator is suitable for steam-water separation operation with the liquid drop diameter larger than 200 mu m, and for a vacuum dehydration process, water cannot be well separated, so that the production efficiency and the normal operation of equipment are seriously influenced.
Disclosure of Invention
The present invention is directed to solving the problems described above. It is an object of the present invention to provide a turbine vacuum system and a steam-water separator thereof that solve the above problems. Specifically, the invention provides a steam-water separator for a turbine vacuum system and the turbine vacuum system, which can operate in an energy-saving and efficient manner.
According to the purpose of the invention, the invention provides a steam-water separator for a turbine vacuum system, which comprises a cylinder, a filtrate pump, a vertical baffle plate sleeved in the cylinder and an inclined baffle plate positioned at the bottom of the vertical baffle plate, wherein the side wall of the cylinder is provided with an air inlet, the top of the cylinder is provided with an air outlet, and the air outlet is communicated with the turbine vacuum pump; the bottom of the barrel is provided with a water outlet, the filtrate pump is communicated with the water outlet, and the inclined direction of the inclined baffle plate faces the water outlet; an annular circulation space is formed between the vertical baffle and the cylinder body; at least one of the inner wall of the cylinder body, the inner wall and the outer wall of the vertical baffle is provided with a plurality of V-shaped flow deflectors, and the opening direction of the V-shaped flow deflectors is consistent with the flow direction of the air flow in the cylinder body.
The vertical baffle is of an annular structure, the side wall of the vertical baffle is provided with a notch, and the notch of the vertical baffle deviates from the air inlet.
The inner wall of the cylinder body, the inner wall and the outer wall of the vertical baffle are respectively provided with a plurality of V-shaped guide vanes.
The opening direction of the V-shaped guide vane on the inner wall of the vertical baffle is opposite to that of the V-shaped guide vane on the outer wall of the vertical baffle.
The opening direction of the V-shaped flow deflector on the inner wall of the cylinder body is consistent with that of the V-shaped flow deflector on the outer wall of the vertical baffle.
The V-shaped guide vanes are arranged in n rows, and the V-shaped guide vanes in adjacent rows are staggered, wherein n is an integer larger than 1.
Wherein, the included angle between the inclined baffle and the horizontal plane is 3-5 degrees.
The steam-water separator further comprises a liquid level meter, and the liquid level meter is in signal connection with the filtrate pump.
And the V-shaped guide vane is fixed through the inserting holes.
According to another aspect of the invention, there is also provided a turbine vacuum system comprising a steam-water separator as described above.
The steam-water separator of the invention utilizes the annular vertical baffle and the V-shaped flow deflectors distributed on the inner wall of the cylinder body to guide and divide the airflow, fully realizes steam-water separation, has high separation efficiency and small energy loss, and the inclined baffle at the bottom of the cylinder body is favorable for thorough liquid drainage and is suitable for being used in a turbine vacuum system.
Other characteristic features and advantages of the invention will become apparent from the following description of exemplary embodiments, which is to be read in connection with the accompanying drawings.
Drawings
The accompanying drawings, which are incorporated in and constitute a part of the specification, illustrate embodiments of the invention and together with the description, serve to explain the principles of the invention. In the drawings, like reference numerals are used to indicate like elements. The drawings in the following description are directed to some, but not all embodiments of the invention. For a person skilled in the art, other figures can be derived from these figures without inventive effort.
FIG. 1 schematically illustrates a structural view of a steam-water separator of the present invention;
FIG. 2 schematically illustrates an internal structure of the steam separator of the present invention;
FIG. 3 schematically illustrates the outer wall layout of the vertical baffles after deployment;
FIG. 4 schematically illustrates the inner wall layout of the vertical baffles after deployment;
fig. 5 exemplarily shows a structural schematic diagram of the inner wall of the barrel after the side wall is unfolded.
Detailed Description
In order to make the objects, technical solutions and advantages of the embodiments of the present invention clearer, the technical solutions in the embodiments of the present invention will be clearly and completely described below with reference to the 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. All other embodiments, which can be derived by a person skilled in the art from the embodiments given herein without making any creative effort, shall fall within the protection scope of the present invention. It should be noted that the embodiments and features of the embodiments in the present application may be arbitrarily combined with each other without conflict.
Aiming at the operation of a turbine vacuum system in a vacuum dehydration process, the inventor designs a steam-water separator which simultaneously conducts flow guiding and flow dividing by utilizing a V-shaped flow guide sheet so as to realize steam-water separation. The annular vertical baffle is arranged inside the barrel of the steam-water separator, the V-shaped flow deflectors are arranged on the inner wall of the barrel, the inner wall of the vertical baffle and the outer wall of the barrel at intervals, the opening direction of the V-shaped flow deflectors faces to the flow direction of air flow, the flow guiding and the flow dividing are realized by utilizing the side walls of the V-shaped flow deflectors, the steam-water separation is realized in the process of impacting the air flow and the V-shaped flow deflectors, the separation efficiency is high, and the energy loss is small. In addition, the bottom of the barrel is provided with an inclined baffle towards the water outlet so as to ensure sufficient liquid drainage and be beneficial to the cleaning and maintenance of the steam-water separator.
The turbine vacuum system and the steam-water separator thereof provided by the invention are explained in detail below with reference to the accompanying drawings.
Fig. 1 shows a schematic structural diagram of a steam-water separator for a turbine vacuum system according to the present invention, fig. 2 shows a schematic structural diagram of the interior of the steam-water separator, and in combination with fig. 1 and fig. 2, the steam-water separator includes a cylinder 1, a filtrate pump 2, a vertical baffle plate 3 sleeved in the cylinder 1, and an inclined baffle plate 4 located at the bottom of the vertical baffle plate 3. The side wall of the cylinder body 1 is provided with an air inlet 11, the top of the cylinder body 1 is provided with an air outlet 12, the air outlet 12 is communicated with a turbine vacuum pump, mixed gas enters the cylinder body 1 from the air inlet 11 under the power action of the turbine vacuum pump and then impacts on the vertical baffle 3, and the mixed gas rotates and circulates under the guide of the vertical baffle 3, the inner wall of the cylinder body 1 and the V-shaped flow deflector 5, and simultaneously steam-water separation is completed. A water outlet 13 is arranged at the bottom of the cylinder 1, and the filtrate pump 2 is communicated with the water outlet 13 and used for discharging the liquid after steam-water separation out of the cylinder 1; the inclined baffle 4 is positioned at the bottom of the barrel 1, and the inclined direction of the inclined baffle is arranged towards the water outlet 13, so that sufficient liquid drainage is ensured, and meanwhile, the cleaning and maintenance of the steam-water separator at the later stage are facilitated.
Specifically, an annular flow space is formed between the vertical baffle 3 and the cylinder 1, and the mixed gas enters through the gas inlet 11 and then flows rotationally along the annular flow space. A plurality of V-shaped flow deflectors 5 are arranged on at least one of the inner wall of the cylinder body 1 and the inner wall and the outer wall of the vertical baffle 3 and are used for dividing the main air flow close to each wall surface into a plurality of strands of small air flows, so that steam-water separation is realized. Specifically, the opening direction of the V-shaped flow deflector 5 is consistent with the flow direction of the air flow in the cylinder 1, so that two blades of the V-shaped flow deflector 5 are ensured to guide and divide the air flow, and sufficient steam-water separation is ensured.
In the invention, the vertical baffle 3 is an annular structure with a notch 30 on the side wall, and the notch 30 of the vertical baffle 3 is arranged away from the air inlet 11, so that the air flow flows to the inner wall 302 along the outer wall 301 of the vertical baffle 3 and then is discharged upwards through the air outlet 12, and the spiral rising and separation of the air flow are realized. Illustratively, the arc length of the gap 30 is 1/5-1/3 of the circumference enclosed by the two axial ends of the vertical baffle 3. For example, the arc length of the notch 30 is 1/4 of the circumference enclosed by the two axial ends of the vertical baffle 3, that is, the vertical baffle 3 is 3/4 circumference, and the notch 30 is located in the 180-degree direction of the air inlet 11.
In the embodiment shown in fig. 2, a plurality of V-shaped guide vanes 5 are respectively arranged on the inner wall of the cylinder 1, the outer wall 301 and the inner wall 302 of the vertical baffle 3, so as to improve the flow guiding and flow dividing operation of the air flow and improve the steam-water separation efficiency.
Because the mixed gas is through inside the air inlet 11 entering barrel 1 back, strike the outer wall 301 of erecting baffle 3 and then shunt to both sides, consequently, the opening opposite direction of the V type water conservancy diversion piece 5 that is located air inlet 11 both sides to fully guarantee the water conservancy diversion and the reposition of redundant personnel effect to the air current. And after the air current passes through the annular circulation space between the cylinder 1 and the vertical baffle 3, the air current circulates towards the interior of the vertical baffle 3 from the notch 30 of the vertical baffle 3 and rotationally rises along the inner wall 302 of the vertical baffle 3, so that the opening direction of the V-shaped flow deflector 5 on the inner wall 302 of the vertical baffle 3 is opposite to the opening direction of the V-shaped flow deflector 5 on the outer wall 301 of the vertical baffle 3, and the opening direction of the V-shaped flow deflector 5 on the inner wall of the cylinder 1 is consistent with the opening direction of the V-shaped flow deflector 5 on the outer wall 301 of the vertical baffle 3.
Further, the notch 30 is disposed away from the air inlet 11, so that the V-shaped baffles 5 on the inner wall of the cylinder 1, the outer wall 301 of the vertical baffle 3 and the inner wall 302 thereof are symmetrically arranged from left to right using the air inlet 11 or the position corresponding to the air inlet 11 as a central axis. Fig. 3 shows a specific layout of the V-shaped guide vanes 5 on the outer wall 301 of the vertical baffle 3 after unfolding, fig. 4 shows a specific layout of the V-shaped guide vanes 5 on the inner wall 302 of the vertical baffle 3 after unfolding, and fig. 5 shows a specific layout of the V-shaped guide vanes 5 on the inner wall of the barrel 1 after unfolding the side wall. Referring to fig. 2 to 5, a plurality of V-shaped baffles 5 are arranged in n rows on the inner wall of the cylinder 1, the outer wall 301 and the inner wall 302 of the vertical baffle 3, wherein n is an integer greater than 1. In order to further improve the diversion and flow distribution effects of the V-shaped diversion sheets 5, the V-shaped diversion sheets 5 in adjacent rows are arranged in a staggered mode.
In a specific embodiment, the V-shaped guide vane 5 may be detachably connected, for example, fixed by plugging, for cleaning. Illustratively, a plurality of insertion holes are formed at intervals on the inner wall of the barrel 1 and/or on the outer wall 301 of the vertical baffle 3 and/or on the inner wall 302 of the vertical baffle 3, and the V-shaped guide vanes 5 are inserted and fixed through the insertion holes.
In order to ensure the service life of the steam-water separator and the installation firmness of the vertical baffle 3 and the V-shaped guide vane 5, the vertical baffle 3 can be welded at the bottom of the cylinder body 1, and the V-shaped guide vane 5 can also be welded for reinforcement.
Because the air flow finally flows to the annular middle part of the vertical baffle 3, and the separated air is discharged from the air outlet 12 at the top of the cylinder 1 (above the annular part of the vertical baffle 3), the liquid flows to the bottom of the cylinder 1 along each wall surface (the inner wall of the cylinder 1, the outer wall 301 and the inner wall 302 of the vertical baffle 3) after being separated under the flow guiding and dividing action of the V-shaped flow guide sheet 5, and is finally discharged from the water outlet 13. The inclined baffle 4 is arranged mainly for ensuring that liquid in the annular middle of the vertical baffle 3 is fully discharged, and under the ordinary condition, the included angle between the inclined baffle 4 and the horizontal plane is 3-5 degrees. In other embodiments, the inclined baffle 4 may be extended to the bottom of the annular passage between the vertical baffle 3 and the cylinder 1, and further, the bottom of the cylinder 1 may be provided with an inclined surface facing the water discharge opening 13. The inclined baffle 4 facilitates not only the discharge of separated liquid during operation, but also the discharge of cleaning liquid (e.g. sewage after scouring, etc.) during the cleaning of the steam-water separator.
It should be noted that the steam-water separator of the present invention further includes a liquid level meter 14, the liquid level meter 14 is disposed on the side wall of the barrel 1, the detection end of the liquid level meter 14 is located in the barrel 1, and the liquid level meter 14 is in signal connection with the filtrate pump 2. The liquid level meter 14 is used for detecting the amount of liquid separated from the interior of the cylinder 1 in real time, and when the liquid reaches a preset detection threshold value of the liquid level meter 14, a starting signal is sent to the filtrate pump 2 to start the filtrate pump 2, so that the liquid in the cylinder 1 is discharged, and the normal operation and the working efficiency of the steam-water separator are ensured.
The steam-water separator has the advantages that through the arrangement of the vertical baffle 3 and the V-shaped guide vane 5, the steam-water separation efficiency of mixed gas is high, the energy loss is small, the liquid drainage is convenient, the steam-water separator is suitable for a turbine vacuum system, and is particularly suitable for vacuum dewatering equipment in the wet part of the light industry and papermaking industry.
The invention also provides a turbine vacuum system which is suitable for the steam-water separator and comprises the steam-water separator.
The above-described aspects may be implemented individually or in various combinations, and such variations are within the scope of the present invention.
It should be noted that, in this document, the terms "comprises," "comprising," or any other variation thereof, are intended to cover a non-exclusive inclusion, such that a process, method, article, or apparatus that comprises a list of elements does not include only those elements but may include other elements not expressly listed or inherent to such process, method, article, or apparatus. Without further limitation, an element defined by the phrase "comprising an …" does not exclude the presence of other identical elements in a process, method, article, or apparatus that comprises the element.
Finally, it should be noted that: the above examples are only for illustrating the technical solutions of the present invention, and are not limited thereto. Although the present invention has been described in detail with reference to the foregoing embodiments, it will be understood by those of ordinary skill in the art that: the technical solutions described in the foregoing embodiments may still be modified, or some technical features may be equivalently replaced; and such modifications or substitutions do not depart from the spirit and scope of the corresponding technical solutions of the embodiments of the present invention.
Claims (9)
1. The steam-water separator for the turbine vacuum system is characterized by comprising a cylinder body (1), a filtrate pump (2), a vertical baffle (3) sleeved in the cylinder body (1) and an inclined baffle (4) positioned at the bottom of the vertical baffle (3), wherein a gas inlet (11) is formed in the side wall of the cylinder body (1), a gas outlet (12) is formed in the top of the cylinder body (1), and the gas outlet (12) is communicated with a turbine vacuum pump; a water outlet (13) is formed in the bottom of the barrel (1), the filtrate pump (2) is communicated with the water outlet (13), and the inclined baffle (4) is arranged towards the water outlet (13) in the inclined direction;
an annular circulation space is formed between the vertical baffle (3) and the cylinder body (1); the inner wall of the barrel body (1), the inner wall and the outer wall of the vertical baffle (3) are respectively provided with a plurality of V-shaped flow deflectors (5), and the opening direction of the V-shaped flow deflectors (5) is consistent with the flow direction of the air flow in the barrel body (1).
2. The steam-water separator as claimed in claim 1, characterized in that the vertical baffle (3) is of an annular structure with a gap (30) in the side wall, and the gap (30) of the vertical baffle (3) is arranged away from the air inlet (11).
3. Steam-water separator according to claim 1, characterized in that the opening of the V-shaped deflector (5) on the inner wall of the vertical baffle (3) is directed opposite to the opening of the corresponding V-shaped deflector (5) on the outer wall of the vertical baffle (3).
4. The steam-water separator according to claim 1, characterized in that the opening orientation of the V-shaped guide vanes (5) on the inner wall of the cylinder (1) is in accordance with the opening orientation of the corresponding V-shaped guide vanes (5) on the outer wall of the vertical baffle (3).
5. The steam-water separator as claimed in claim 1, wherein a plurality of said V-shaped baffles (5) are arranged in n rows, and said V-shaped baffles (5) in adjacent rows are staggered, where n is an integer greater than 1.
6. The steam-water separator according to claim 1, characterized in that the angle between the inclined baffle (4) and the horizontal plane is 3 ° -5 °.
7. The steam-water separator according to claim 1, characterized in that it further comprises a level gauge (14), said level gauge (14) being in signal connection with said filtrate pump (2).
8. The steam-water separator as claimed in claim 1, characterized in that the inner wall of the cylinder (1) and/or the vertical baffle (3) is provided with a plug hole through which the V-shaped guide vane (5) is fixed.
9. A turbine vacuum system, characterized in that the turbine vacuum system comprises a steam-water separator according to any one of claims 1 to 8.
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202010464851.7A CN111359313B (en) | 2020-05-28 | 2020-05-28 | Turbine vacuum system and steam-water separator thereof |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202010464851.7A CN111359313B (en) | 2020-05-28 | 2020-05-28 | Turbine vacuum system and steam-water separator thereof |
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| CN111359313A CN111359313A (en) | 2020-07-03 |
| CN111359313B true CN111359313B (en) | 2020-08-21 |
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| CN114837861A (en) * | 2022-03-29 | 2022-08-02 | 哈尔滨工程大学 | V-shaped waterproof structure |
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| DE2430637A1 (en) * | 1973-07-06 | 1975-01-23 | Seco Tools Ab | ARRANGEMENT FOR THE CONDENSATION AND SEPARATION OF WAX, PARFFIN AND OTHER SUBSTANCES FROM A GAS FLOW |
| CN201930646U (en) * | 2010-12-03 | 2011-08-17 | 昆山力诺能源机械有限公司 | Steam-water separating device |
| CN202366579U (en) * | 2011-12-27 | 2012-08-08 | 楚天科技股份有限公司 | Gas-water separation device and rubber plug cleaning machine provided with same |
| CN102639207A (en) * | 2009-11-13 | 2012-08-15 | 埃克森美孚化学专利公司 | Fluid separation sytems and methods |
| JP2015217326A (en) * | 2014-05-15 | 2015-12-07 | 吉雄 網本 | Cyclone type gas-liquid separator having improved gas-liquid separation efficiency |
| CN207438556U (en) * | 2017-10-27 | 2018-06-01 | 北京奥林匹亚锅炉有限公司 | Steam boiler and its steam-water separator |
| CN210044949U (en) * | 2019-04-28 | 2020-02-11 | 武汉友谊食品工程有限公司 | Steam-water separation device |
-
2020
- 2020-05-28 CN CN202010464851.7A patent/CN111359313B/en active Active
Patent Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE2430637A1 (en) * | 1973-07-06 | 1975-01-23 | Seco Tools Ab | ARRANGEMENT FOR THE CONDENSATION AND SEPARATION OF WAX, PARFFIN AND OTHER SUBSTANCES FROM A GAS FLOW |
| CN102639207A (en) * | 2009-11-13 | 2012-08-15 | 埃克森美孚化学专利公司 | Fluid separation sytems and methods |
| CN201930646U (en) * | 2010-12-03 | 2011-08-17 | 昆山力诺能源机械有限公司 | Steam-water separating device |
| CN202366579U (en) * | 2011-12-27 | 2012-08-08 | 楚天科技股份有限公司 | Gas-water separation device and rubber plug cleaning machine provided with same |
| JP2015217326A (en) * | 2014-05-15 | 2015-12-07 | 吉雄 網本 | Cyclone type gas-liquid separator having improved gas-liquid separation efficiency |
| CN207438556U (en) * | 2017-10-27 | 2018-06-01 | 北京奥林匹亚锅炉有限公司 | Steam boiler and its steam-water separator |
| CN210044949U (en) * | 2019-04-28 | 2020-02-11 | 武汉友谊食品工程有限公司 | Steam-water separation device |
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Denomination of invention: A turbine vacuum system and its steam water separator Effective date of registration: 20220525 Granted publication date: 20200821 Pledgee: Weifang Development Branch of Industrial and Commercial Bank of China Ltd. Pledgor: SHANDONG TIANRUI HEAVY INDUSTRY Co.,Ltd. Registration number: Y2022370000051 |
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| PC01 | Cancellation of the registration of the contract for pledge of patent right | ||
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Date of cancellation: 20230509 Granted publication date: 20200821 Pledgee: Weifang Development Branch of Industrial and Commercial Bank of China Ltd. Pledgor: SHANDONG TIANRUI HEAVY INDUSTRY Co.,Ltd. Registration number: Y2022370000051 |
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| PE01 | Entry into force of the registration of the contract for pledge of patent right | ||
| PE01 | Entry into force of the registration of the contract for pledge of patent right |
Denomination of invention: A turbine vacuum system and its steam water separator Effective date of registration: 20230509 Granted publication date: 20200821 Pledgee: Weifang Development Branch of Industrial and Commercial Bank of China Ltd. Pledgor: SHANDONG TIANRUI HEAVY INDUSTRY Co.,Ltd. Registration number: Y2023370000080 |
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| PC01 | Cancellation of the registration of the contract for pledge of patent right | ||
| PC01 | Cancellation of the registration of the contract for pledge of patent right |
Granted publication date: 20200821 Pledgee: Weifang Development Branch of Industrial and Commercial Bank of China Ltd. Pledgor: SHANDONG TIANRUI HEAVY INDUSTRY Co.,Ltd. Registration number: Y2023370000080 |
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| PE01 | Entry into force of the registration of the contract for pledge of patent right | ||
| PE01 | Entry into force of the registration of the contract for pledge of patent right |
Denomination of invention: A turbine vacuum system and its steam water separator Granted publication date: 20200821 Pledgee: Weifang Development Branch of Industrial and Commercial Bank of China Ltd. Pledgor: SHANDONG TIANRUI HEAVY INDUSTRY Co.,Ltd. Registration number: Y2024370000012 |