Spray drying tower for mixing hard alloy rod powder

By designing a spray drying tower, utilizing a blower to heat the air and a cyclone separator to recover the exhaust gas, the problem of powder uniformity and purity control in the preparation of cemented carbide rod powder was solved, thereby improving the alloy's forming performance and production efficiency.

CN223760421UActive Publication Date: 2026-01-06SUZHOU RUISEN CEMENTED CARBIDE
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Patent Information

Application Number
CN202520093163.2
Authority / Receiving Office
CN · China
Patent Type
Utility models(China)
Current Assignee / Owner
Filing Date
2025-01-15
Publication Date
2026-01-06
Estimated Expiration
2035-01-15

AI Technical Summary

Technical Problem

Existing technologies make it difficult to effectively control the uniformity and purity of powders during the preparation of cemented carbide rod powders, which affects the alloy's performance and formability.

Method used

A spray drying tower is used. The filtered air is heated by a blower and an air heater and then delivered to the drying chamber. The liquid material is sent to the atomizing nozzle through a liquid delivery pump and a liquid delivery pipe to be atomized and dried by contact with the hot air. A cyclone separator and a bag filter separate and recover the exhaust gas and fine powder.

Benefits of technology

This method enables the control of uniformity and purity of cemented carbide rod powder, improves the alloy's formability and density, simplifies the production process, and reduces manual intervention and costs.

✦ Generated by Eureka AI based on patent content.

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Abstract

The utility model relates to the technical field of drying, and discloses a spray drying tower for mixing hard alloy rod powder materials, which comprises a drying chamber, the bottom of the drying chamber is provided with a discharge port I, and the top of the drying chamber is provided with a fixing hole; the first supporting column is arranged on the outer wall of the drying chamber. Through the air feeder and the air heater, air filtered by the air filter is sucked in through operation of the air feeder, then the air is conveyed into the air heater through the air supply pipe to be heated, the heated air is conveyed into the drying chamber through the air inlet pipe, at the moment, the liquid feeding pump is started, and the liquid is conveyed into the drying chamber. The liquid feeding pump operates to suck feed liquid in the feed liquid tank through the liquid suction pipe, then the feed liquid is conveyed into the atomizing nozzle through the liquid conveying pipe, then the atomizing nozzle is started to atomize the feed liquid and spray the feed liquid out to make contact with hot air in the drying chamber, and therefore the effect that fog drops are rapidly dried into powder under the action of the hot air and fall into the first collecting bottle is achieved.
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Description

Technical Field

[0001] This utility model relates to the field of drying technology, specifically a spray drying tower for mixing cemented carbide rod powder. Background Technology

[0002] Cemented carbide rods, also known as tungsten carbide rods, are composite materials produced by powder metallurgy, consisting of refractory metal compounds and binder metals. Cemented carbide rod powder is the raw material for manufacturing cemented carbide rods, mainly composed of hard compounds of refractory metals and binder metal powders. Cemented carbide has a hardness second only to diamond and possesses very high compressive and bending strength. Due to its excellent properties, cemented carbide rods are widely used in many fields: cutting tools, such as lathe tools, milling cutters, planing tools, drill bits, boring tools, etc., for cutting various metals and non-metals; mining tools, used in mining and tunneling operations; measuring tools, used to manufacture measuring instruments and precision parts; and wear-resistant parts, used to manufacture components that need to withstand high wear, such as cylinder liners and precision bearings.

[0003] Spray drying technology is characterized by its rapid drying speed, completing the drying process in just a few seconds. This makes the preparation of cemented carbide rod powder more efficient, significantly shortening the production cycle. Furthermore, the operation and control of the spray drying tower are convenient, simplifying the production process and reducing manual intervention and production costs. During this process, the particle size, purity, and uniformity of the powder can be well controlled. For cemented carbide, the uniformity and purity of the powder have a significant impact on the alloy's performance. The spray drying tower ensures uniform powder distribution and high purity, thereby improving the formability and density of cemented carbide.

[0004] Therefore, a spray drying tower for mixing cemented carbide rod powder is proposed. Utility Model Content

[0005] The purpose of this invention is to provide a spray drying tower for mixing cemented carbide rod powder, so as to solve the problems mentioned in the background art.

[0006] To achieve the above objectives, this utility model provides the following technical solution: a spray drying tower for mixing cemented carbide rod powder, comprising a drying chamber, a discharge port at the bottom of the drying chamber, and a fixing hole at the top of the drying chamber; a support column disposed on the outer wall of the drying chamber; a collection bottle disposed at the bottom of the drying chamber; an atomizing nozzle disposed within the fixing hole in the drying chamber; a drying assembly disposed on the outside of the drying chamber; and a recycling and processing assembly disposed on the back of the drying chamber; wherein the drying assembly includes: a feeding section disposed on one side of the drying chamber; and an air inlet section disposed on the other side of the drying chamber.

[0007] Preferably, the outer wall of the drying chamber is fixedly connected to the top of the support column, the collection bottle is adapted to the discharge port, and the outer wall of the atomizing nozzle is fixedly connected to the inner wall of the fixing hole.

[0008] Preferably, the feeding part includes: a liquid tank, which is set on one side of the drying chamber, and a feeding hole is opened on the top of the liquid tank; a top cover is provided in the feeding hole of the liquid tank; a liquid delivery pump is fixedly connected to the top of the liquid tank; a suction pipe is connected to the bottom of the liquid delivery pump; and a delivery pipe is connected to the top of the liquid delivery pump.

[0009] Preferably, one end of the suction tube passes through the top of the liquid tank and extends into the interior, and one end of the delivery tube is connected to the top of the atomizing nozzle.

[0010] This feeding section effectively delivers the liquid material to the atomizing nozzle.

[0011] Preferably, the air inlet includes: a blower, disposed on the other side of the drying chamber; an air filter is connected to one side of the blower, an air supply pipe is connected to the other side of the blower, an air heater is connected to one end of the air supply pipe, and an air inlet pipe is connected to the top of the air heater.

[0012] Preferably, one end of the air inlet pipe is connected to the outer wall of the drying chamber, and a filter screen is provided on the inner wall of one end of the air inlet pipe.

[0013] This air inlet can effectively deliver hot air into the drying room.

[0014] Preferably, the recycling and processing component includes: a cyclone separator disposed on the back of the drying chamber, with a discharge port two at the bottom of the cyclone separator; a support column two fixedly connected to the outer wall of the cyclone separator; a connecting pipe one connected to the outer wall of the cyclone separator; a collection bottle two disposed at the bottom of the cyclone separator; a connecting pipe two connected to the top of the cyclone separator; a bag filter connected to one end of the connecting pipe two; a support column three fixedly connected to the outer wall of the bag filter; a collection bottle three disposed at the bottom of the bag filter; a suction pipe connected to the back of the bag filter; an exhaust fan connected to one end of the suction pipe; and an exhaust pipe connected to one side of the exhaust fan.

[0015] Preferably, one end of the connecting pipe is connected to the outer wall of the drying chamber, the collecting bottle is adapted to the discharge port, and the bottom of the bag filter is provided with a discharge port, the collecting bottle is adapted to the discharge port.

[0016] This recycling and processing component can effectively recover and process exhaust gas and fine powder.

[0017] This invention provides a spray drying tower for mixing cemented carbide rod powder. It has the following beneficial effects:

[0018] (1) This utility model uses a blower and an air heater. The blower draws in the air filtered by the air filter and then delivers it to the air heater through the air supply pipe for heating. The heated air is then delivered to the drying chamber through the air inlet pipe. At this time, the liquid delivery pump is started. The liquid delivery pump draws in the liquid from the liquid tank through the liquid suction pipe and then delivers it to the atomizing nozzle through the liquid delivery pipe. The atomizing nozzle is then started to atomize the liquid and spray it out to contact the hot air in the drying chamber, thereby achieving the effect that the droplets are quickly dried into powder under the action of the hot air and fall into the collection bottle.

[0019] (2) By starting the cyclone separator, the operation of the cyclone separator draws in the exhaust gas and fine powder in the drying chamber through the connecting pipe one and separates them, so that the fine powder falls into the collection bottle two. The exhaust gas is transported to the bag filter through the connecting pipe two and then filtered through the bag filter. Then the exhaust fan is started to draw in the filtered gas through the suction pipe and then discharge it through the exhaust pipe, thereby achieving the effect of recycling and treating the exhaust gas and fine powder. Attached Figure Description

[0020] Figure 1 This is a perspective view of the present utility model;

[0021] Figure 2 This is a schematic cross-sectional view of the present invention.

[0022] Figure 3 This is a side view of the present invention;

[0023] Figure 4 This is a rear view of the present invention.

[0024] In the diagram: 1 Drying chamber, 2 Support column one, 3 Collection bottle one, 4 Atomizing nozzle, 5 Drying assembly, 51 Feeding section, 511 Liquid tank, 512 Top cover, 513 Liquid pump, 514 Suction pipe, 515 Infusion pipe, 52 Air inlet, 521 Blower, 522 Air filter, 523 Air duct, 524 Air heater, 525 Air inlet pipe, 6 Recycling and processing assembly, 611 Cyclone separator, 612 Support column two, 613 Connecting pipe one, 614 Collection bottle two, 615 Connecting pipe two, 616 Bag filter, 617 Support column three, 618 Collection bottle three, 619 Suction pipe, 6110 Exhaust fan, 6111 Exhaust pipe. Detailed Implementation

[0025] The technical solutions of the present utility model will be clearly and completely described below with reference to the accompanying drawings of the embodiments. Obviously, the described embodiments are only some embodiments of the present utility model, and not all embodiments. Based on the embodiments of the present utility model, all other embodiments obtained by those of ordinary skill in the art without creative effort are within the protection scope of the present utility model.

[0026] Examples of the embodiments are shown in the accompanying drawings, wherein the same or similar reference numerals denote the same or similar elements or elements having the same or similar functions throughout. The embodiments described below with reference to the accompanying drawings are exemplary and intended to explain the present invention, and should not be construed as limiting the present invention. Example

[0027] A preferred embodiment of the spray drying tower for mixing cemented carbide rod powder provided by this utility model is as follows: Figure 1-4 As shown: A spray drying tower for mixing cemented carbide rod powder includes a drying chamber 1, with a discharge port at the bottom and a fixing hole at the top; a support column 2, disposed on the outer wall of the drying chamber 1; a collection bottle 3, disposed at the bottom of the drying chamber 1; an atomizing nozzle 4, disposed in the fixing hole of the drying chamber 1; a drying assembly 5, disposed on the outside of the drying chamber 1; and a recycling assembly 6, disposed on the back of the drying chamber 1. The drying assembly 5 includes: a feeding part 51, disposed on one side of the drying chamber 1; and an air inlet part 52, disposed on the other side of the drying chamber 1.

[0028] The outer wall of the drying chamber 1 is fixedly connected to the top of the support column 2, the collection bottle 3 is adapted to the discharge port 1, and the outer wall of the atomizing nozzle 4 is fixedly connected to the inner wall of the fixing hole.

[0029] The feeding section 51 includes: a liquid tank 511, which is located on one side of the drying chamber 1. The top of the liquid tank 511 is provided with a feeding hole. A top cover 512 is provided in the feeding hole of the liquid tank 511. A liquid delivery pump 513 is fixedly connected to the top of the liquid tank 511. A suction pipe 514 is connected to the bottom of the liquid delivery pump 513. A delivery pipe 515 is connected to the top of the liquid delivery pump 513.

[0030] One end of the suction pipe 514 passes through the top of the liquid tank 511 and extends into the interior, while one end of the delivery pipe 515 is connected to the top of the atomizing nozzle 4.

[0031] The air inlet 52 includes: a blower 521, which is located on the other side of the drying chamber 1; an air filter 522 is connected to one side of the blower 521, and an air supply duct 523 is connected to the other side of the blower 521. An air heater 524 is connected to one end of the air supply duct 523, and an air inlet duct 525 is connected to the top of the air heater 524.

[0032] One end of the air inlet duct 525 is connected to the outer wall of the drying chamber 1, and a filter screen is provided on the inner wall of one end of the air inlet duct 525.

[0033] Furthermore, in this embodiment, the operation of the blower 521 and the air heater 524 allows the blower 521 to draw in the air filtered by the air filter 522, and then deliver it to the air heater 524 for heating through the air supply pipe 523. The heated air is then delivered to the drying chamber 1 through the air inlet pipe 525. At this time, the liquid delivery pump 513 is started. The operation of the liquid delivery pump 513 draws in the liquid from the liquid tank 511 through the liquid suction pipe 514, and then delivers it to the atomizing nozzle 4 through the liquid delivery pipe 515. The atomizing nozzle 4 is then started to atomize the liquid and spray it out to contact the hot air in the drying chamber 1, thereby achieving the effect that the droplets are quickly dried into powder under the action of the hot air and fall into the collection bottle 3. Example

[0034] Based on Embodiment 1, a preferred embodiment of the spray drying tower for mixing cemented carbide rod powder provided by this utility model is as follows: Figure 1-4 As shown: The recycling and processing component 6 includes: a cyclone separator 611, which is located on the back of the drying chamber 1, and a discharge port 2 is provided at the bottom of the cyclone separator 611; a support column 2 612 is fixedly connected to the outer wall of the cyclone separator 611, a connecting pipe 1 613 is connected to the outer wall of the cyclone separator 611, a collection bottle 2 614 is provided at the bottom of the cyclone separator 611, a connecting pipe 2 615 is connected to the top of the cyclone separator 611, a bag filter 616 is connected to one end of the connecting pipe 2 615, a support column 3 617 is fixedly connected to the outer wall of the bag filter 616, a collection bottle 3 618 is provided at the bottom of the bag filter 616, a suction pipe 619 is connected to the back of the bag filter 616, an exhaust fan 6110 is connected to one end of the suction pipe 619, and an exhaust pipe 6111 is connected to one side of the exhaust fan 6110.

[0035] One end of the connecting pipe 613 is connected to the outer wall of the drying chamber 1. The collection bottle 614 is adapted to the discharge port 2. The bottom of the bag filter 616 is provided with the discharge port 3. The collection bottle 618 is adapted to the discharge port 3.

[0036] Furthermore, in this embodiment, by activating the cyclone separator 611, the operation of the cyclone separator 611 draws in the exhaust gas and fine powder in the drying chamber 1 through the connecting pipe 613 and separates them, causing the fine powder to fall into the collection bottle 614. The exhaust gas is then transported to the bag filter 616 through the connecting pipe 615, where it is filtered. The exhaust fan 6110 is then activated to draw in the filtered gas through the suction pipe 619 and discharge it through the exhaust pipe 6111, thereby achieving the effect of recovering and treating the exhaust gas and fine powder.

[0037] In operation, the blower 521 draws in air filtered by the air filter 522 and delivers it to the air heater 524 via the air supply pipe 523 for heating. The heated air is then delivered to the drying chamber 1 via the air inlet pipe 525. At this time, the liquid delivery pump 513 is started, drawing liquid from the liquid tank 511 through the suction pipe 514 and delivering it to the atomizing nozzle 4 via the delivery pipe 515. The atomizing nozzle 4 is then started to atomize the liquid and spray it out to contact the hot air in the drying chamber 1. This causes the droplets to dry rapidly into powder under the action of hot air and fall into collection bottle 3. When the cyclone separator 611 is started, the operation of the cyclone separator 611 draws in the exhaust gas and fine powder in the drying chamber 1 through the connecting pipe 613 and separates them, so that the fine powder falls into collection bottle 614. The exhaust gas is transported to the bag filter 616 through the connecting pipe 615 and then filtered through the bag filter 616. Then the exhaust fan 6110 is started to draw in the filtered gas through the suction pipe 619 and then discharge it through the exhaust pipe 6111, thereby achieving the recovery and treatment of exhaust gas and fine powder.

[0038] Finally, it should be noted that the above description is merely a preferred embodiment of this utility model and is not intended to limit the utility model. Although the utility model has been described in detail with reference to the foregoing embodiments, those skilled in the art can still modify the technical solutions described in the foregoing embodiments or make equivalent substitutions for some of the technical features. Any modifications, equivalent substitutions, improvements, etc., made within the spirit and principles of this utility model should be included within the protection scope of this utility model.

Claims

1. A spray drying tower for mixing a cemented carbide rod powder, characterized in that, Including dry room (1), the bottom of dry room (1) is provided with discharge port one, the top of dry room (1) is provided with fixed hole; Support column one (2) is arranged on the outer wall of dry room (1); Collecting bottle one (3) is arranged at the bottom of dry room (1); Atomizing nozzle (4) is arranged in the fixed hole of dry room (1); Dry assembly (5) is arranged outside dry room (1); Recycling processing assembly (6) is arranged on the back of dry room (1); Wherein, dry assembly (5) includes: Feeding site (51) is arranged on one side of dry room (1); Air inlet site (52) is arranged on the other side of dry room (1).

2. A spray drying tower for mixing cemented carbide rod powder according to claim 1, characterized in that: The outer wall of dry room (1) is fixedly connected with the top of support column one (2), collecting bottle one (3) is matched with discharge port one, the outer wall of atomizing nozzle (4) is fixedly connected with the inner wall of fixed hole.

3. A spray drying tower for mixing cemented carbide rod powder according to claim 1, characterized in that: The feeding site (51) includes: Liquid tank (511) is arranged on one side of dry room (1), the top of liquid tank (511) is provided with feeding hole; Top cover (512) is arranged in the feeding hole of liquid tank (511), the top of liquid tank (511) is fixedly connected with liquid pump (513), the bottom of liquid pump (513) is communicated with suction tube (514), the top of liquid pump (513) is communicated with liquid delivery tube (515).

4. A spray drying tower for mixing cemented carbide rod powder according to claim 3, characterized in that: One end of suction tube (514) penetrates the top of liquid tank (511) and extends to the inside, one end of liquid delivery tube (515) is communicated with the top of atomizing nozzle (4).

5. A spray drying tower for mixing cemented carbide rod powder according to claim 1, characterized in that: The air inlet site (52) includes: Air blower (521) is arranged on the other side of dry room (1); Air filter (522) is communicated on one side of air blower (521), air delivery pipe (523) is communicated on the other side of air blower (521), one end of air delivery pipe (523) is communicated with air heater (524), air heater (524) is communicated with air inlet pipe (525) on the top.

6. A spray drying tower for mixing cemented carbide rod powder according to claim 5, characterized in that: One end of air inlet pipe (525) is communicated with the outer wall of dry room (1), the inner wall of one end of air inlet pipe (525) is provided with filter screen.

7. A spray drying tower for mixing cemented carbide rod powder according to claim 1, characterized in that: The recycling processing assembly (6) includes: Cyclone separator (611) is arranged on the back of dry room (1), the bottom of cyclone separator (611) is provided with discharge port two; The outer wall of the cyclone separator (611) is fixedly connected with a supporting column two (612), the outer wall of the cyclone separator (611) is communicatively provided with a communicating pipe one (613), the bottom of the cyclone separator (611) is provided with a collecting bottle two (614), the top of the cyclone separator (611) is communicatively provided with a communicating pipe two (615), one end of the communicating pipe two (615) is communicatively provided with a cloth bag filter (616), the outer wall of the cloth bag filter (616) is fixedly connected with a supporting column three (617), the bottom of the cloth bag filter (616) is provided with a collecting bottle three (618), the back of the cloth bag filter (616) is communicatively provided with a suction pipe (619), one end of the suction pipe (619) is communicatively provided with an exhaust fan (6110), one side of the exhaust fan (6110) is communicatively provided with an exhaust pipe (6111).

8. A spray drying tower for mixing cemented carbide rod powder according to claim 7, characterized in that: One end of the communicating pipe one (613) is communicatively provided with the outer wall of the drying chamber (1), the collecting bottle two (614) is matched with the second discharge port, the bottom of the cloth bag filter (616) is provided with a discharge port three, and the collecting bottle three (618) is matched with the discharge port three.