A steam-water separation type boiler with a steam flow rate control function
By separating the integrated evaporation structure and automatically adjusting the water vapor flow rate components, the problems of parts damage and improper flow rate control in the steam boiler are solved, efficient steam-water separation and energy utilization are achieved, and the stability and safety of the equipment are improved.
Patent Information
- Application Number
- CN202510216925.8
- Authority / Receiving Office
- CN · China
- Patent Type
- Patents(China)
- Current Assignee / Owner
- Filing Date
- 2025-02-26
- Publication Date
- 2025-07-04
- Estimated Expiration
- 2045-02-26
AI Technical Summary
During the steam and water separation process, equipment parts of existing steam boilers are prone to damage, improper flow rate control leads to water and steam loss and energy waste, and may bring out harmful substances, affecting the safety and environment of the equipment.
The integrated structure of separation and evaporation is adopted, combined with components such as sliding feed tank, separator, flow control chamber and return pipeline, and efficient steam separation and energy utilization are achieved by automatically adjusting the water and steam flow rate and spoiler barrier.
Reduce damage to equipment parts, improve service life, enhance equipment stability and energy utilization efficiency, reduce the risk of water vapor escape, and reduce the emission of harmful substances.
Smart Images

Figure CN119802572B_ABST
Abstract
Description
Technical Field
[0001] The present invention relates to the technical field of steam boilers, and specifically to a steam-water separation type boiler with a steam flow rate control function. Background Art
[0002] A steam boiler refers to a boiler device for producing steam. Steam boilers can be classified into electric steam boilers, oil-fired steam boilers, gas-fired steam boilers, etc. according to the fuel. Among these types of boilers, they are further divided into two types, one is a vertical boiler and the other is a horizontal boiler. During the process of producing steam, a large amount of steam is usually generated, and the steam will also carry some water vapor to flow. At this time, attention should be paid to the problem of steam-water separation. Usually, manufacturers will use steam-water separation equipment to process it, which is a device for separating gas and liquid in a liquid-containing system. At the same time, a suitable set of steam traps is connected to the drain port at the bottom of the steam-water separator. The advantages are high water removal efficiency and small volume.
[0003] Using a steam-water separator and a steam boiler is a common method for those skilled in the art. However, such a combination will inevitably result in too many redundant parts of the equipment, which will greatly increase the probability of equipment failure. Especially for such equipment in a high-temperature state, the lifespan of the parts is shorter than that of ordinary parts, which will lead to greater safety problems during the operation of the equipment. Secondly, during the production process, if the flow rate control is not proper, it will also cause a large amount of water vapor to be lost, resulting in the inability to fully utilize energy, and it may also carry out some harmful substances, bringing irreversible effects to the external environment. Summary of the Invention
[0004] The purpose of the present invention is to provide a steam-water separation type boiler with a steam flow rate control function to solve the problems raised in the prior art.
[0005] To achieve the above-mentioned purpose, the present invention provides the following technical solutions: The present invention provides a technical solution, the steam-water separation boiler includes a steam boiler, a heating chamber is arranged in the steam boiler, a sliding feed trough is arranged in the heating chamber, a heating furnace body is slidably connected in the sliding feed trough, an exhaust port is arranged on the steam boiler, a water inlet and a water exchange port are arranged in the steam boiler, a separator is arranged in the steam boiler, a collecting port is arranged on the separator, a reflux pipe is arranged on the separator, a filtering component is arranged in the reflux pipe, a plurality of heat exchange plates are arranged on the heating furnace body, each heat exchange plate is respectively provided with an output pipe, and a control Valve, a heating tank is arranged in the heating furnace body, and a tumbling assembly is arranged in the heating tank. When working, water is first added to the water inlet, and then fuel is added to the sliding feed tank, and then the fuel is ignited to heat the heating tank. During the heating process, the clean water will be evaporated, and the evaporated water vapor will carry some water vapor into the separator, and the separator will screen and aggregate the water vapor and water vapor, and then the water vapor that has not been condensed will be discharged from the exhaust port. During the heating process, the heat exchange plate can work selectively, which can not only utilize energy, but also cool the separator, so that the ability to intercept water vapor is improved.
[0006] A combustion aid is arranged in the heating furnace body, a heat transfer plate is arranged on the heating furnace body, a plurality of transfer protrusions are arranged on the heat transfer plate, a plurality of transfer grooves are arranged at the bottom of the heating groove, the positions and shapes of the transfer grooves correspond to the transfer protrusions, a lifting track is arranged at the bottom of the steam boiler, a sliding wheel is arranged at the bottom of the heating furnace body, the sliding wheel is embedded in the lifting track and is slidably connected with the lifting track, when heating, the combustion aid is used to ignite the fuel in the sliding feed trough, the sliding feed trough slides on the lifting track until the sliding feed trough and the heat transfer plate are close to the maximum limit, and the sliding wheel has a lubricating effect, and a lifting wedge surface is arranged on the lifting track, so that the sliding feed trough can be raised and lowered, and then the sliding feed trough is locked for stable combustion.
[0007] The separator includes a separation chamber shell, a fitting strip is provided on the separation chamber shell, a fitting groove is provided on the inner wall of the steam boiler, the fitting strip is embedded in the fitting groove and is slidably connected with the fitting groove, a locking nut is provided on the fitting groove, the collecting port is connected with the separation chamber shell, a separation assembly and a flow control chamber are provided in the separation chamber shell, and when performing separation, the position of the separation chamber shell needs to be determined, the locking nut slides in the fitting groove, thereby resisting the fitting strip and completing the position locking operation, while the separation assembly and the flow control chamber respectively realize the effects of separation and flow velocity control.
[0008] A collection plate and a diversion groove are arranged in the flow control chamber. The collection plate is rotatably connected to the diversion groove. A lifting groove is arranged on the collection plate. A plurality of flow disturbing plates are arranged in the diversion groove. Each flow disturbing plate is slidably connected to the diversion groove. A wedge-shaped plate is arranged in the diversion groove. The wedge-shaped plate is slidably connected to the diversion groove. The upper surface of the wedge-shaped plate is in sliding contact with the bottom end of the flow disturbing plate. After water vapor and steam enter the flow control chamber, the collection plate will block part of the water vapor and gather it in the lifting groove. When the water in the lifting groove accumulates to a certain extent, it will drive the collection plate to rotate on the diversion groove and squeeze the internal wedge-shaped plate, and the wedge-shaped plate will drive the flow disturbing plate to slide. When the water vapor is large, the rising speed and swinging frequency of the lifting groove will increase accordingly. Correspondingly, the lifting frequency of the flow disturbing plate will also increase, and the disturbance and blocking effects on the water vapor flowing through the flow control chamber will also be enhanced.
[0009] A reset elastic sheet is arranged on the wedge-shaped plate. The end of the reset elastic sheet away from the wedge-shaped plate abuts against the inside of the diversion groove. The end of the wedge-shaped plate away from the reset elastic sheet is in sliding contact with the collection plate. The lifting groove is slidably connected to the bottom end of the collection plate. A plurality of through holes are arranged on the collection plate. The through holes are through holes with an "S" shape. The setting of the reset elastic sheet can realize the reciprocating movement of the wedge-shaped plate, so as to realize the continuous lifting effect of the flow disturbing plate. Through the through holes with a specific shape, the rapid blocking and gathering of water vapor can be realized, and the blocking response can be made faster.
[0010] A support wheel is arranged at the bottom end of each flow disturbing plate. The support wheel is in sliding contact with the upper end surface of the wedge-shaped plate. A plurality of return holes are respectively arranged on each flow disturbing plate. Aggregation spines are respectively arranged in the return holes. A push link group is rotatably connected to the bottom end of the wedge-shaped plate. The push link group is slidably connected to the inner wall of the flow control chamber. A guide block is arranged at the end of the push link group away from the wedge-shaped plate. The guide block is slidably connected to the collection port. The setting of the support wheel can make the sliding of the flow disturbing plate on the wedge-shaped plate smoother. The return holes on the flow disturbing plate can collect the water vapor, and the aggregation spines can make the water vapor drip faster, also avoiding the condensation of internal water droplets and the occurrence of dryness phenomena, reducing energy loss.
[0011] The separation component includes a separation chamber. The separation chamber is communicated with the flow control chamber. One end of the separation chamber away from the flow control chamber is communicated with the exhaust port. A polymerization mesh plate is arranged at the upper end of the separation chamber. A wave plate is rotatably connected to the polymerization mesh plate. A plurality of rotating inclined holes are arranged on the wave plate. The wave plate is rotatably connected to the polymerization mesh plate. A polymerization groove is arranged at the bottom end of the separation chamber. The polymerization groove is communicated with the return pipeline through a connecting valve. After the separation of water vapor and steam is completed, they enter the separation chamber together with water. Subsequently, the steam will enter the exhaust port through the polymerization mesh plate. As the steam flows, the wave plate on the polymerization mesh plate will rotate. Under the action of the rotating inclined holes, the steam is screened for the last time, and the screened water is sent into the separation chamber and waits to flow back to the heating tank.
[0012] A reflux vortex plate is arranged inside the reflux pipeline. The reflux vortex plate is rotatably connected to the reflux pipeline. A surging push rod is rotatably connected to the reflux vortex plate. The surging push rod is slidably connected to the heating tank. A surging plate is arranged inside the heating tank. A pushing wedge block is arranged at one end of the surging push rod away from the reflux vortex plate. The pushing wedge block is in sliding contact with one end of the surging plate. After the water vapor gathers and enters the separation chamber, it will exert pressure on the reflux vortex plate. The reflux vortex plate will rotate and drive the surging push rod to swing. The surging push rod slides on the heating tank, and the surging push rod drives the pushing wedge block to slide reciprocally. Under the action of the pushing wedge block, the surging plate will slide inside the heating tank.
[0013] A driving gear is rotatably connected to the pushing wedge block. Tooth teeth are arranged at the bottom end of the heating tank. The driving gear meshes with the tooth teeth. A rotating shaft is arranged on the driving gear. The rotating shaft is rotatably connected to the surging push rod. A plurality of crushing frames are arranged on the pushing wedge block. The crushing frames are rotatably connected to the pushing wedge block. The crushing frames are in sliding contact with the heating tank. When the driving gear rotates, under the action of the tooth teeth at the bottom end of the heating tank, the driving gear will drive the pushing wedge block to slide. After the pushing wedge block moves on the heating tank, the crushing frames above it will also swing on the pushing wedge block, so as to achieve the effect of surging and crushing the sludge in the heating tank, and reduce the problem of reduced heat transfer efficiency caused by the aggregation of sludge and sediment.
[0014] Compared with the prior art, the beneficial effects of the present invention are:
[0015] 1. The present invention adopts a structure integrating separation and evaporation, reducing the problem of component damage that may occur during the operation of the equipment, improving the service life of the equipment, and at the same time enabling better separation of water vapor and reducing the problem of reflux wall hanging.
[0016] 2. The present invention adopts a structural component with the function of automatically adjusting the water vapor flow rate according to the evaporation amount. By detecting the blocking amount of water vapor, the flow rate is automatically adjusted to fully disturb and intercept the water vapor, so that the water vapor can be fully absorbed, reducing the problem of water vapor escaping under different conditions and enhancing the stability of the equipment.
[0017] 3. The present invention adopts an automatic surging structural component, using the reflux power to stir the water in the heating tank, reducing the equipment cost. At the same time, it adopts a gear-driven structure to reduce the surging resistance. At the same time, the turned-up soil and sediment also reduce the problem of heat blocking, enhancing the use efficiency of the equipment. BRIEF DESCRIPTION OF THE DRAWINGS
[0018] Figure 1 is a three-dimensional structural schematic diagram of the present invention;
[0019] Figure 2 is a schematic diagram of the internal structure of the steam boiler of the present invention;
[0020] Figure 3 is Figure 2 a schematic structural diagram of the locally enlarged B in
[0021] Figure 4 is Figure 2 a schematic structural diagram of the locally enlarged A in
[0022] Figure 5 a schematic side sectional structure diagram of the present invention;
[0023] Figure 6 a schematic partial sectional structure diagram of the collection plate of the present invention;
[0024] Figure 7 a schematic partial sectional structure diagram of the spoiler of the present invention;
[0025] Figure 8 a schematic sectional structure diagram of the separation chamber of the present invention.
[0026] In the figure: 1, steam boiler; 2, heating chamber; 3, sliding feed chute; 4, heating furnace body; 5, exhaust port; 6, water inlet; 7, water change port; 8, separator; 9, collection port; 10, return pipeline; 11, filter assembly; 12, heat exchange plate; 13, output pipeline; 14, control valve; 15, heating tank; 16, tumbling assembly; 401, combustor; 402, heat transfer plate; 403, transfer protrusion; 404, transfer groove; 405, rising track; 406, sliding wheel; 801, separation chamber shell; 802, fitting strip; 803, fitting groove; 804, locking nut; 17, separation component; 18, flow control chamber; 1801, collection plate; 1802, lifting groove; 1803, spoiler; 1804, wedge plate; 1805, reset spring piece; 1806, through hole; 1807, support wheel; 1808, return hole; 1809, polymerization spike; 1810, push link group; 1811, flow guide block; 1701, separation chamber; 1703, polymerization wire mesh; 1704, fluctuation plate; 1705, rotating inclined hole; 1706, polymerization groove; 1001, return vortex plate; 1002, surging push rod; 1003, surging plate; 1004, push wedge; 1005, push gear; 1006, rotating shaft; 1007, crushing rack. Detailed implementation manners
[0027] Next, the technical solutions in the embodiments of the present invention will be clearly and completely described in conjunction with the accompanying drawings in the embodiments of the present invention. Obviously, the described embodiments are only a part of the embodiments of the present invention, rather than all the embodiments. Based on the embodiments of the present invention, all other embodiments obtained by those of ordinary skill in the art without creative efforts shall fall within the protection scope of the present invention.
[0028] Embodiment: As Figures 1 - 8 shown, the present invention provides a technical solution. The steam-water separation boiler includes a steam boiler 1, a heating chamber 2 is arranged inside the steam boiler 1, a sliding feed chute 3 is arranged inside the heating chamber 2, a heating furnace body 4 is slidably connected inside the sliding feed chute 3, an exhaust port 5 is arranged on the steam boiler 1, a water inlet 6 and a water changing port 7 are arranged inside the steam boiler 1, a separator 8 is arranged inside the steam boiler 1, a collection port 9 is arranged on the separator 8, a reflux pipeline 10 is arranged on the separator 8, a filtering component 11 is arranged inside the reflux pipeline 10, a plurality of heat exchange plates 12 are arranged on the heating furnace body 4, an output pipeline 13 is respectively arranged inside each heat exchange plate 12, a control valve 14 is arranged on the output pipeline 13, a heating tank 15 is arranged inside the heating furnace body 4, a tumbling component 16 is arranged inside the heating tank 15. When working, first inject water into the water inlet 6, then add fuel into the sliding feed chute 3, then ignite the fuel to heat the heating tank 15. During the heating process, the clear water will be evaporated, and the evaporated water vapor will carry some water vapor into the separator 8. The separator 8 will screen and aggregate the water vapor and the water vapor. Then, the uncondensed water vapor will be discharged from the exhaust port 5. During the heating process, the heat exchange plates 12 can work selectively, which can not only utilize energy but also cool the separator 8, so as to improve the ability to intercept water vapor.
[0029] A combustor 401 is arranged inside the heating furnace body 4, a heat transfer plate 402 is arranged on the heating furnace body 4, a plurality of transfer protrusions 403 are arranged on the heat transfer plate 402, a plurality of transfer grooves 404 are arranged at the bottom end of the heating tank 15, and the positions and shapes of the transfer grooves 404 correspond to those of the transfer protrusions 403. A rising track 405 is arranged at the bottom end of the steam boiler 1, a sliding wheel 406 is arranged at the bottom end of the heating furnace body 4, and the sliding wheel 406 is embedded in the rising track 405 and is slidably connected with the rising track 405. When heating, use the combustor 401 to ignite the fuel in the sliding feed chute 3, and the sliding feed chute 3 slides on the rising track 405 until the sliding feed chute 3 is closest to the heat transfer plate 402. The sliding wheel 406 plays a lubricating role, and a rising wedge surface is arranged on the rising track 405, so that the sliding feed chute 3 can be lifted and lowered. Then, lock the sliding feed chute 3 to ensure stable combustion.
[0030] The separator 8 includes a separation chamber housing 801, on which there is a fitting strip 802. On the inner wall of the steam boiler 1, there is a fitting groove 803. The fitting strip 802 is inserted into the fitting groove 803 and is slidably connected to the fitting groove 803. A locking nut 804 is provided on the fitting groove 803. The collection port 9 is communicated with the separation chamber housing 801. A separation component 17 and a flow control chamber 18 are arranged in the separation chamber housing 801. When separating, it is necessary to determine the position of the separation chamber housing 801. The locking nut 804 slides in the fitting groove 803, thus abutting against the fitting strip 802 and completing the position locking operation. The separation component 17 and the flow control chamber 18 respectively achieve the effects of separation and control of the flow rate.
[0031] A collection plate 1801 and a diversion groove are arranged in the flow control chamber 18. The collection plate 1801 is rotatably connected to the diversion groove. A lifting groove 1802 is provided on the collection plate 1801. A plurality of spoiler plates 1803 are arranged in the diversion groove. Each spoiler plate 1803 is slidably connected to the diversion groove respectively. A wedge plate 1804 is arranged in the diversion groove. The wedge plate 1804 is slidably connected to the diversion groove. The upper surface of the wedge plate 1804 is in sliding contact with the bottom ends of the spoiler plates 1803. After the water vapor and steam enter the flow control chamber 18, the collection plate 1801 will block part of the water vapor and gather it in the lifting groove 1802. When the water in the lifting groove 1802 gathers to a certain extent, it will drive the collection plate 1801 to rotate on the diversion groove and squeeze the internal wedge plate 1804, and the wedge plate 1804 drives the spoiler plates 1803 to slide. When the water vapor is large, the rising speed and swinging frequency of the lifting groove 1802 will increase accordingly. Correspondingly, the lifting frequency of the spoiler plates 1803 will also increase, and the disturbance and blocking effects on the water vapor flowing through the flow control chamber 18 will be strengthened.
[0032] A reset elastic sheet 1805 is arranged on the wedge plate 1804. One end of the reset elastic sheet 1805 away from the wedge plate 1804 abuts against the inside of the diversion groove. One end of the wedge plate 1804 away from the reset elastic sheet 1805 is in sliding contact with the collection plate 1801. The lifting groove 1802 is slidably connected to the bottom end of the collection plate 1801. A plurality of through holes 1806 are provided on the collection plate 1801. The through holes 1806 are through holes with an "S" shape. The arrangement of the reset elastic sheet 1805 can realize the reciprocating movement of the wedge plate 1804, thus realizing the continuous lifting effect of the spoiler plates 1803. Through the through holes with a specific shape, the rapid blocking and gathering of the water vapor can be realized, and the blocking response can be made faster.
[0033] At the bottom end of each spoiler 1803, there is a support wheel 1807. The support wheel 1807 is in sliding contact with the upper end surface of the wedge-shaped plate 1804. A plurality of return holes 1808 are respectively formed in each spoiler 1803, and polymerization spikes 1809 are respectively arranged in the return holes 1808. The bottom end of the wedge-shaped plate 1804 is rotatably connected with a push link group 1810. The push link group 1810 is in sliding connection with the inner wall of the flow control chamber 18. At one end of the push link group 1810 away from the wedge-shaped plate 1804, there is a flow guide block 1811. The flow guide block 1811 is in sliding connection with the collection port 9. The setting of the support wheel 1807 can make the sliding of the spoiler 1803 on the wedge-shaped plate 1804 smoother. The return holes 1808 on the spoiler 1803 can collect water vapor, and the polymerization spikes 1809 can make the water vapor drip faster, also avoiding the condensation of internal water droplets and the occurrence of dry phenomena, reducing energy loss.
[0034] The separation component 17 includes a separation chamber 1701. The separation chamber 1701 is communicated with the flow control chamber 18. One end of the separation chamber 1701 away from the flow control chamber 18 is communicated with the exhaust port 5. A polymerization mesh disk 1703 is arranged at the upper end of the separation chamber 1701. A wave plate 1704 is rotatably connected to the polymerization mesh disk 1703. A plurality of rotating inclined holes 1705 are formed in the wave plate 1704. The wave plate is rotatably connected to the polymerization mesh disk 1703. A polymerization groove 1706 is arranged at the bottom end of the separation chamber 1701. The polymerization groove 1706 is communicated with the return pipeline 10 through a connection valve. After the separation of water vapor and water vapor is completed, they enter the separation chamber 1701 together with water. Subsequently, the water vapor will enter the exhaust port 5 through the polymerization mesh disk 1703. As the water vapor flows, the wave plate 1704 on the polymerization mesh disk 1703 will rotate. Under the action of the rotating inclined holes 1705, the water vapor is screened for the last time, and the screened water is sent into the separation chamber 1701 and waits to flow back to the heating tank 15.
[0035] A return vortex plate 1001 is arranged in the return pipeline 10. The return vortex plate 1001 is rotatably connected to the return pipeline 10. A tumbling push rod 1002 is rotatably connected to the return vortex plate 1001. The tumbling push rod 1002 is in sliding connection with the heating tank 15. A tumbling plate 1003 is arranged in the heating tank 15. At one end of the tumbling push rod 1002 away from the return vortex plate 1001, there is a push wedge 1004. The push wedge 1004 is in sliding contact with one end of the tumbling plate 1003. After the water vapor gathers and enters the separation chamber 1701, it will exert pressure on the return vortex plate 1001. The return vortex plate 1001 will rotate and drive the tumbling push rod 1002 to swing. The tumbling push rod 1002 slides on the heating tank 15, and the tumbling push rod 1002 drives the push wedge 1004 to slide reciprocally. Under the action of the push wedge 1004, the tumbling plate 1003 will slide in the heating tank 15.
[0036] A driving wedge is rotatably connected with a driving gear 1005. Teeth are provided at the bottom end of the heating tank 15. The driving gear 1005 meshes with the teeth. A rotating shaft 1006 is provided on the driving gear 1005. The rotating shaft 1006 is rotatably connected with a surging push rod 1002. A plurality of crushing frames 1007 are provided on the driving wedge 1004. The crushing frames 1007 are rotatably connected with the driving wedge 1004. The crushing frames 1007 are in sliding contact with the heating tank 15. When the driving gear 1005 rotates, under the action of the teeth at the bottom end of the heating tank 15, the driving wedge 1004 will be driven to slide. After the driving wedge 1004 moves on the heating tank 15, the crushing frames 1007 above it will also swing on the driving wedge 1004, so as to realize the effect of surging and crushing the sludge in the heating tank 15, and reduce the problem of reduced heat transfer efficiency caused by the aggregation of sludge and sediment.
[0037] Working principle: Prepare the equipment, adjust the position of the separator 8. Slide the locking nut 804 in the fitting groove 803 to abut against the fitting strip 802 and complete the position locking operation. Then, fill water into the water inlet 6 and add fuel into the sliding feed tank 3. Use the combustor 401 to ignite the fuel in the sliding feed tank 3. The sliding feed tank 3 slides on the lifting track 405 to heat the heating tank 15. During the heating process, the clear water will be evaporated, and the evaporated water vapor will carry some water vapor into the separator 8. After the water vapor and water vapor enter the flow control chamber 18, the collecting plate 1801 will block part of the water vapor and gather it in the lifting tank 1802. When the water in the lifting tank 1802 gathers to a certain extent, it will drive the collecting plate 1801 to rotate on the diversion groove and squeeze the internal wedge plate 1804, and the wedge plate 1804 will drive the turbulence plate 1803 to slide. Then, the uncondensed water vapor will be discharged from the exhaust port 5. During the heating process, the water vapor will enter the exhaust port 5 through the polymerization mesh disk 1703. As the water vapor flows, the wave plate 1704 on the polymerization mesh disk 1703 will rotate. Under the action of the rotating inclined hole 1705, the water vapor will be screened for the last time. When the water vapor gathers and enters the separation chamber 1701, it will exert pressure on the reflux vortex plate 1001. The reflux vortex plate 1001 will rotate and drive the surging push rod 1002 to swing. Under the action of the teeth at the bottom end of the heating tank 15, the driving gear 1005 will drive the driving wedge 1004 to slide, and the crushing frame 1007 will also crush the sediment. The heat exchange plate 12 can work selectively to cool the separator 8, so as to improve the ability to intercept water vapor.
[0038] For those skilled in the art, it is obvious that the present invention is not limited to the details of the above-described exemplary embodiments, and the present invention can be implemented in other specific forms without departing from the spirit or essential characteristics of the present invention. Therefore, from any point of view, the embodiments should be regarded as exemplary and non-restrictive. The scope of the present invention is defined by the appended claims rather than the above description. Therefore, all changes falling within the meaning and scope of the equivalent elements of the claims are intended to be embraced within the present invention. Any reference signs in the claims should not be construed as limiting the claims involved.
Claims
1. A steam-water separation boiler with a steam flow rate control function, characterized in that: The steam-water separation type boiler includes a steam boiler (1), a heating chamber (2) is arranged inside the steam boiler (1), a sliding feed chute (3) is arranged inside the heating chamber (2), a heating furnace body (4) is slidably connected inside the sliding feed chute (3), an exhaust port (5) is arranged on the steam boiler (1), a water inlet (6) and a water changing port (7) are arranged inside the steam boiler (1), a separator (8) is arranged inside the steam boiler (1), a collection port (9) is arranged on the separator (8), a reflux pipeline (10) is arranged on the separator (8), a filtering component (11) is arranged inside the reflux pipeline (10), a plurality of heat exchange plates (12) are arranged on the heating furnace body (4), an output pipeline (13) is respectively arranged inside each heat exchange plate (12), a control valve (14) is arranged on the output pipeline (13), a heating tank (15) is arranged inside the heating furnace body (4), and a tumbling component (16) is arranged inside the heating tank (15); The separator (8) includes a separation chamber shell (801), a fitting strip (802) is arranged on the separation chamber shell (801), a fitting groove (803) is arranged on the inner wall of the steam boiler (1), the fitting strip (802) is embedded into the fitting groove (803) and is slidably connected with the fitting groove (803), a locking nut (804) is arranged on the fitting groove (803), the collection port (9) is communicated with the separation chamber shell (801), and a separation component (17) and a flow control chamber (18) are arranged inside the separation chamber shell (801); A collection plate (1801) and a flow dividing groove are arranged inside the flow control chamber (18), the collection plate (1801) is rotatably connected with the flow dividing groove, a lifting groove (1802) is arranged on the collection plate (1801), a plurality of flow disturbing plates (1803) are arranged inside the flow dividing groove, each flow disturbing plate (1803) is respectively slidably connected with the flow dividing groove, a wedge-shaped plate (1804) is arranged inside the flow dividing groove, the wedge-shaped plate (1804) is slidably connected with the flow dividing groove, and the upper surface of the wedge-shaped plate (1804) is in sliding contact with the bottom end of the flow disturbing plate (1803).
2. The steam-water separation boiler with a steam flow rate control function according to claim 1, characterized in that: A combustor (401) is arranged inside the heating furnace body (4), a heat transfer plate (402) is arranged on the heating furnace body (4), a plurality of transfer protrusions (403) are arranged on the heat transfer plate (402), a plurality of transfer grooves (404) are arranged at the bottom end of the heating tank (15), the positions and shapes of the transfer grooves (404) correspond to those of the transfer protrusions (403), a rising track (405) is arranged at the bottom end of the steam boiler (1), and a sliding wheel (406) is arranged at the bottom end of the heating furnace body (4), and the sliding wheel (406) is embedded into the rising track (405) and is slidably connected with the rising track (405).
3. A steam-water separation boiler with a steam flow rate control function according to claim 1, characterized in that: A reset elastic piece (1805) is arranged on the wedge-shaped plate (1804). One end of the reset elastic piece (1805) far from the wedge-shaped plate (1804) abuts against the shunt groove. One end of the wedge-shaped plate (1804) far from the reset elastic piece (1805) is in sliding contact with the collecting plate (1801). The lifting groove (1802) is slidably connected to the bottom end of the collecting plate (1801). A plurality of through holes (1806) are arranged on the collecting plate (1801), and the through holes (1806) are through holes with an "S" shape.
4. A steam-water separation type boiler with a steam flow rate control function according to claim 3, characterized in that: A support wheel (1807) is arranged at the bottom end of each spoiler (1803). The support wheel (1807) is in sliding contact with the upper end surface of the wedge-shaped plate (1804). A plurality of return holes (1808) are respectively formed in each spoiler (1803), and polymerization spikes (1809) are respectively arranged in the return holes (1808). A push link group (1810) is rotatably connected to the bottom end of the wedge-shaped plate (1804). The push link group (1810) is in sliding contact with the inner wall of the flow control chamber (18). A flow guide block (1811) is arranged at one end of the push link group (1810) far from the wedge-shaped plate (1804), and the flow guide block (1811) is in sliding contact with the collection port (9).
5. The steam-water separation boiler with a steam flow rate control function according to claim 4, characterized in that: The separation assembly (17) includes a separation chamber (1701). The separation chamber (1701) is communicated with the flow control chamber (18). One end of the separation chamber (1701) far from the flow control chamber (18) is communicated with the exhaust port (5). A polymerization mesh plate (1703) is arranged at the upper end of the separation chamber (1701). A wave plate (1704) is rotatably connected to the polymerization mesh plate (1703). A plurality of rotating inclined holes (1705) are formed in the wave plate (1704). The wave plate (1704) is rotatably connected to the polymerization mesh plate (1703). A polymerization groove (1706) is arranged at the bottom end of the separation chamber (1701), and the polymerization groove (1706) is communicated with the return pipeline (10) through a communication valve.
6. The steam-water separation boiler with a steam flow rate control function according to claim 1, characterized in that: A return vortex plate (1001) is arranged in the return pipeline (10). The return vortex plate (1001) is rotatably connected to the return pipeline (10). A surging push rod (1002) is rotatably connected to the return vortex plate (1001). The surging push rod (1002) is in sliding contact with the heating groove (15). A surging plate (1003) is arranged in the heating groove (15). A push wedge (1004) is arranged at one end of the surging push rod (1002) far from the return vortex plate (1001), and the push wedge (1004) is in sliding contact with one end of the surging plate (1003).
7. The steam-water separation type boiler with a steam flow rate control function according to claim 6, characterized in that: A driving gear (1005) is rotatably connected to the driving wedge block. Teeth are provided at the bottom end of the heating groove (15). The driving gear (1005) meshes with the teeth. A rotating shaft (1006) is provided on the driving gear (1005). The rotating shaft (1006) is rotatably connected to the surging push rod (1002). A plurality of crushing frames (1007) are provided on the driving wedge block (1004). The crushing frames (1007) are rotatably connected to the driving wedge block (1004), and the crushing frames are in sliding contact with the heating groove (15).
Citation Information
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