High-moisture sludge ultra-fine synchronizing deep-drying device and a method thereof

Patent metadata

Field	Value
Publication number	US-11286192-B2
Application number	US-202016824659-A
Country	US
Kind code	B2
Filing date	Mar 19, 2020
Priority date	Mar 28, 2019
Publication date	Mar 29, 2022
Grant date	Mar 29, 2022

Abstract

The present invention discloses a high-moisture sludge ultra-fine synchronizing deep-drying device and a method thereof. The device has a sludge ultrafine pulverizing unit and a sludge drying unit arranged horizontally in parallel, and a pulverized sludge discharge port arranged between them. The sludge ultrafine pulverizing unit comprises a sludge pulverizing chamber and a sludge feeding port, and the sludge pulverizing chamber is a hollow cylindrical structure with a pulverizing rotation shaft arranged in the center, and the pulverizing rotation shaft is provided with a sludge pulverizing impeller. The lower part of the sludge feeding port is provided with a first baffle and/or a second deflector. The sludge is pulverized into sludge powders in the sludge pulverizing chamber, and then fed into the sludge drying chamber to be fluidized and dried. The present invention has the advantage of high drying efficiency, etc.

First claim

We claim:

1. A high-moisture sludge ultra-fine synchronizing deep-drying device, comprising a sludge ultrafine pulverizing unit and a sludge drying unit juxtaposed horizontally, and a pulverized sludge discharge port arranged between the sludge ultrafine pulverizing unit and the sludge drying unit;
wherein, the sludge ultrafine pulverizing unit comprises a sludge pulverizing chamber and a sludge feeding port arranged at one end of the sludge pulverizing chamber, and the sludge pulverizing chamber is a hollow cylindrical structure with a pulverizing rotation shaft horizontally arranged in the center, and the pulverizing rotation shaft is provided with a sludge pulverizing impeller;
the sludge drying unit comprises a sludge drying chamber and a fluidizing rotation shaft arranged at a lower part of the sludge drying chamber, the fluidizing rotation shaft is arranged horizontally and coaxial with the pulverizing rotation shaft; and the fluidizing rotation shaft is provided with a fluidizing impeller;
an upper part of the sludge drying chamber is provided with a mixing rotation shaft arranged horizontally, a plurality of mixing impellers are provided on the mixing rotation shaft, and the upper part of the sludge drying chamber is further provided with an air inlet located below the mixing impellers; and
a lower part of the sludge drying chamber is provided with a dried sludge outlet arranged at a side away from the pulverized sludge discharge port; and the fluidized rotation shaft is arranged through the dried sludge outlet.

2. The device of claim 1 , wherein, the sludge pulverizing impeller comprises a plurality of blades uniformly arranged in a concentric circle with the pulverizing rotation shaft as the center, and an angle χ of 0° to 25° is formed between each of the blades and the axial direction of the pulverizing rotating shaft.

3. The device of claim 1 , wherein, two or more sets of sludge pulverizing impellers are arranged along an axial direction of the pulverizing rotation shaft.

4. The device of claim 1 , wherein, a guiding baffle is vertically arranged at a lower part of the sludge feeding port near a side of the sludge pulverizing impeller.

5. The device of claim 1 , wherein, the lower part of the sludge feeding port is provided with a first deflector which is located above the pulverizing rotation shaft, and the first deflector is inclined downward along the traveling direction of the sludge with an inclination angle α of 15° to 30°.

6. The device of claim 4 , wherein, the lower part of the sludge feeding port is provided with a second deflector, which is located below the pulverizing rotation shaft, and the second deflector is inclined downward along the traveling direction of the sludge with an inclination angle β of 15° to 60°.

7. The device of claim 1 , wherein, a pulverizing sludge guiding member is annularly disposed on an inner wall of the sludge pulverizing chamber, the pulverizing sludge guiding member has a right-angled trapezoidal section, and the pulverizing sludge guiding member is arranged inside the pulverized sludge discharge port.

8. The device of claim 1 , wherein the device comprises several sludge drying chambers arranged in parallel, and the fluidized rotation shaft horizontally passes through the lower portion of the sludge drying chambers.

9. The device of claim 1 , wherein, the dried sludge outlet is provided with a moving guiding module and a fixed guiding module; the fixed guiding module is semi-annularly disposed at the bottom of the sludge drying chamber, and an upper portion of the fixed guiding module is provided with a guiding slope that contracts toward the outlet direction; and the moving guiding module is a block that is capable of moving up and down.

10. The device of claim 1 , wherein, the guiding slope has an inclination angle η of 45° to 70°.

11. The device of claim 1 , wherein, there are at least two fluidizing impellers arranged axially along the fluidizing rotation shaft; each fluidizing impeller comprises a plurality of fluidizing blades, and an axial angle ε of 0° to 10° is formed between the fluidized blades and the fluidizing rotation shaft.

12. The device of claim 1 , wherein, each of the mixing impellers comprises a plurality of mixing blades, and an axial angle φ of 0° to 15° is formed between the mixing blades and the mixing rotation shaft.

13. The device of claim 1 , further comprising a separation collection chamber arranged behind the sludge drying chamber.

14. A method of sludge ultra-fine synchronizing deep-drying by using the sludge ultra-fine synchronous deep drying device of claim 1 , comprising:
pulverizing high-moisture sludge into coarse sludge particles which are fed into the sludge pulverizing chamber through the sludge feeding port, and adjusting rotation speed of the pulverizing rotation shaft to pulverize the sludge coarse particles passing the sludge pulverizing impellers into sludge powders, and transferring the sludge powders upon the pulverizing rotation shaft to the pulverized sludge discharge port as rotation of the pulverizing rotation shaft and pushing the sludge powders into the sludge drying chamber from the pulverized sludge discharge port;
adjusting rotation speed of the fluidized rotation shaft, so that the sludge powders are fluidized in the sludge drying chamber under a disturbance of the fluidizing impeller; and introducing dry air from an air inlet to mix it with the fluidized sludge powders in the sludge drying chamber and dry the sludge powders;
adjusting rotation speed of the mixing rotation shaft, so that the fluidized sludge powders in the sludge drying chamber are uniformly mixed with the dry air, and the sludge powders are sufficiently dried to become dried sludge powders and discharged from the dried sludge outlet; and
separating and collecting the dried sludge powders.

15. The method of claim 14 , wherein, the sludge ultra-fine synchronizing deep-drying device has several sludge drying chambers arranged in parallel, forming a multi-stage sludge drying chamber comprising at least a first sludge drying chamber, a second sludge drying chamber, and/or a last sludge drying chamber, and the method further comprises:
pulverizing high-moisture sludge into coarse sludge particles which are fed into the sludge pulverizing chamber through the sludge feeding port, and adjusting the rotation speed of the pulverizing rotation shaft to pulverize the sludge coarse particles passing the sludge pulverizing impellers into sludge powders, and transferring the sludge powders upon the pulverizing rotation shaft to the pulverized sludge discharge port as rotation of the pulverizing rotation shaft, and pushing the sludge powders into the first sludge drying chamber from the pulverized sludge discharge port;
adjusting the rotation speed of the fluidized rotation shaft, so that the sludge powders are fluidized in the first sludge drying chamber under the disturbance of the fluidizing impeller; and introducing dry air from an air inlet to mix with the fluidized sludge powders in the first sludge drying chamber and dry the sludge powders;
adjusting the rotation speed of the mixing rotation shaft, so that the fluidized sludge powders in the first sludge drying chamber are uniformly mixed with the dry air, and the sludge powders are sufficiently dried to become dried sludge powders;
allowing the dried sludge powders from the dried sludge outlet of the first sludge drying chamber into the second sludge drying chamber, and repeating the above drying process in the second sludge drying chamber until dried sludge powders are obtained and discharged from th

Assignees

• Univ Beijing Science & Technology
• Shengshi Weilan Shandong Environmental Science & Tech Co Ltd
• Shengshi Weilan Shandong Envi Sci & Tech Co Ltd

Inventors

• Xing Yi
• Hong Chen
• Si Yanxiao
• Su Wei
• Jiang Bo

Classifications

• C02F2301/08

  Multistage treatments, e.g. repetition of the same process step under different conditions · CPC title

• C02F11/13 Primary

  by heating · CPC title

• F26B3/0923

  by mechanical means, e.g. vibrated plate, stirrer · CPC title

• F26B5/041

  for drying flowable materials, e.g. suspensions, bulk goods, in a continuous operation, e.g. with locks or other air tight arrangements for charging/discharging · CPC title

• F26B17/26

  with movement performed by reciprocating or oscillating conveyors propelling materials over stationary surfaces; with movement performed by reciprocating or oscillating shelves, sieves, or trays {(F26B17/006 takes precedence)} · CPC title