IP Library Granted Patent US 10,279,287
Granted Patent B2
US 10,279,287 · App. 15/110,538 · Granted May 7, 2019

Equipment for solid-liquid separation and drying of fine-powder slurry, and method therfor

Inventors: Yoichi Nakata (Tokyo, JP); Tomonori Watarai (Tokyo, JP); Sumito Sato (Tokyo, JP); Satoshi Suwa (Tokyo, JP); Tomoki Homma (Tokyo, JP)
Assignee: TSUKISHIMA KIKAI CO., LTD.
B01D33/642B01D33/666F26B5/14F26B17/02F26B17/28F26B17/32
View Patent ↗
Loading inventors, assignments & file history…
Monitor This Case
Get email alerts when status or documents change.
Order Certified Copies
Most orders are placed with the USPTO same day — all within 24 business hours.
Order via The Patent Place →
Pre-filled with this patent's details
Quick Facts
Patent No.
US 10,279,287
App. No.
15/110,538
Granted
May 7, 2019
Kind
B2
Abstract

Prevention of contamination of a dried product, deformation of particles, and a change of particle size distribution. The system includes: a solid-liquid separator in which a processing material is supplied between a pair of endless separation filter cloths wound around an outer periphery of a separation roll, and is dehydrated by being squeezed therebetween and also by ventilation gas passing from a ventilation port formed in an outer peripheral surface of the separation roll; and a horizontal rotary dryer provided on a subsequent stage of the solid-liquid separator, wherein carrier gas is made to flow in a rotating shell of the dryer in a cocurrent manner in the same direction as a conveyance direction of the processing material.

Claims (21)

1. A system for solid-liquid separation and drying of fine-powder slurry, comprising:

a solid-liquid separator including a structure

in which a pair of endless separation filter cloths is wound in a stacked state around an outer periphery of a separation roll rotated in a circumferential direction and is capable of running along the rotation direction of the separation roll, and

in which a processing material supplied between the pair of separation filter cloths is deliquored by being sandwiched and squeezed between the pair of separation filter cloths on an outer peripheral surface of the separation roll and also by ventilation gas passing from an inside toward an outside of the separation roll through a ventilation port formed in the outer peripheral surface of the separation roll; and

a horizontal rotary dryer which is installed on a subsequent stage of the solid-liquid separator, has a feed port of the processing material at one end side and a discharge port of the processing material at another end side, includes: a rotating shell rotatable around an axial direction; and a heating unit provided inside the rotating shell and having heating tubes having a heating medium flow therethrough, and heats and dries the processing material by the heating unit in a process where the processing material supplied from the feed port of the rotating shell is discharged from the discharge port,

wherein carrier gas is made to flow in the rotating shell in a cocurrent manner in the same direction as a conveyance direction of the processing material, a bag filter is provided in a discharge flow path of the carrier gas of the horizontal rotary dryer, an exhaust hood, which is connected to the bag filter and an end portion on the other end side, discharges exhaust gas, and the exhaust hood includes a heating pipe.

2. The system for solid-liquid separation and drying of fine-powder slurry according to claim 1 , wherein a belt conveyor is provided between the solid-liquid separator and the feed port of the horizontal rotary dryer.

3. The system for solid-liquid separation and drying of fine-powder slurry according to claim 2 , wherein a damper is provided between a discharge port of the belt conveyor and the feed port of the horizontal rotary dryer, and the carrier gas is made to flow in from a side closer to the horizontal rotary dryer than the damper.

4. The system for solid-liquid separation and drying of fine-powder slurry according to claim 1 , comprising a downflow path which leads the processing material discharged from the solid-liquid separator of the fine-powder slurry to the feed port of the horizontal rotary dryer by gravity of fall without using a mechanical conveying means.

5. The system for solid-liquid separation and drying of fine-powder slurry according to claim 4 , wherein the downflow path leads the processing material to the feed port of the horizontal rotary dryer only by the gravity of fall.

6. The system for solid-liquid separation and drying of fine-powder slurry according to claim 4 , wherein an airlock device which blocks and permits the communication between an inside of a hood wrapping the solid-liquid separator and an inside of the horizontal rotary dryer is provided in the downflow path.

7. The system for solid-liquid separation and drying of fine-powder slurry according to claim 6 , wherein the airlock device is a plurality of dampers provided in a dropping direction of the processing material.

8. The system for solid-liquid separation and drying of fine-powder slurry according to claim 6 , wherein the airlock device is a rotary valve provided in a dropping direction of the processing material.

9. The system for solid-liquid separation and drying of fine-powder slurry according to claim 6 , wherein a vibration generator is provided on the downflow path.

10. A solid-liquid separation and drying method of fine-powder slurry, the method comprising:

separating a processing material by a solid-liquid separator including a structure in which a pair of endless separation filter cloths is wound in a stacked state around an outer periphery of a separation roll rotated in a circumferential direction and is capable of running along the rotation direction of the separation roll, and a processing material supplied between the pair of separation filter cloths is deliquored by being sandwiched and squeezed between the pair of separation filter cloths on an outer peripheral surface of the separation roll and also by ventilation gas passing from a ventilation port formed in the outer peripheral surface of the separation roll; and

drying the processing material having undergone the solid-liquid separation, by a horizontal rotary dryer which has a feed port of the processing material at one end side and a discharge port of the processing material at another end side, includes: a rotating shell rotatable around an axial direction; and a heating unit provided inside the rotating shell and having heating tubes having a heating medium flow therethrough, and heats and dries the processing material by the heating unit in a process where the processing material supplied from the feed port of the rotating shell is discharged from the discharge port,

wherein carrier gas is made to flow in the rotating shell in a cocurrent manner in the same direction as a conveyance direction of the processing material, a bag filter is provided in a discharge flow path of the carrier gas of the horizontal rotary dryer, an exhaust hood, which is connected to the bag filter and an end portion on the other end side, discharges exhaust gas, and the exhaust hood includes a heating pipe.

11. The solid-liquid separation and drying method of fine-powder slurry according to claim 10 , wherein the processing material discharged from the solid-liquid separator of the fine-powder slurry is led to the feed port of the horizontal rotary dryer by gravity of fall through a downflow path without using a mechanical conveying means.

12. The solid-liquid separation and drying method of fine-powder slurry according to claim 10 , wherein the processing material contains fine particles with a 100 μm particle size or less.

13. The solid-liquid separation and drying method of fine-powder slurry according to claim 10 , wherein the solid-liquid separator includes a cleaning device, and after the processing material having undergone the solid-liquid separation is discharged, a cleaning liquid at a 10° C. to 50° C. temperature is sprayed to the processing material adhering to the separation filter cloth.

Assignments (3)
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Feb 24, 2025
From: TSUKISHIMA HOLDINGS CO.,LTD.
To: TSUKISHIMA KIKAI CO.,LTD.
Reel/Frame 070301/0675 →
CHANGE OF NAME Recorded Feb 19, 2025
From: TSUKISHIMA KIKAI CO.,LTD.
To: TSUKISHIMA HOLDINGS CO.,LTD.
Reel/Frame 070255/0308 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Aug 9, 2016
From: NAKATA, YOICHI; WATARAI, TOMONORI; SATO, SUMITO; SUWA, SATOSHI; HOMMA, TOMOKI
To: TSUKISHIMA KIKAI CO., LTD
Reel/Frame 039381/0246 →
Priority Claims (2)
JP 2014-002930 · Jan 10, 2014 · national
JP 2014-002931 · Jan 10, 2014 · national
Continuity (1)
Related Publication 20160325209A1 · Nov 10, 2016