# US 5,343,630 A · Fiberglass recycling system

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- Number: US 5,343,630 A
- Document ID: US5343630A
- Status: Granted
- Kind: A
- Application number: 07/877,888
- Filed: 1992-05-01
- Granted: 1994-09-06
- Earliest claimed: 1992-05-01
- Inventors: John H. Ferguson, Sr.
- Web page: https://patentgrep.com/patent/US5343630A

## CPC

- F26B 5/08: by centrifugal treatment
- F26B: DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM (drying devices for combines A01D41/133; racks for drying fruit or vegetables A01F25/12; drying foodstuffs A23; drying hair A45D20/00; body-drying implements A47K10/00; drying household articles A47L; drying gases or vapours B01D; chemical or physical processes for dewatering or like separating liquids from solids B01D43/00; centrifugal apparatus B04; drying ceramics C04B33/30; drying yarns or fabrics in association with some other form of treatment D06C; drying frames for laundry without heating or positive air circulation, domestic laundry-or spin-driers, wringing or hot pressing laundry D06F; furnaces, kilns, ovens F27)

## Abstract

A system used to recycle remnant fiberglass that has been removed from bobbins by water jets. The fiberglass recycling system includes a conveyor system for transporting the fiberglass to a centrifuge which dewaters wetted fiberglass. A detector having photoelectric devices is positioned at a discharge end of the conveyor system to detect dimensions of clusters of fiberglass conveyed past the discharge section of the conveyor. The detector is connected to a control unit which calculates the approximate amount of fiberglass conveyed past the detector and deposited into the centrifuge. In response to the amount of fiberglass detected, the control unit directs the operation and timing of the recycle system by selectively controlling the speed of the centrifuge and by placing the conveyor system between a discharge mode and an accumulation mode. A screen condenser is connected to the centrifuge by a conduit and a fan causes dewatered fiberglass in the centrifuge to be drawn through the conduit to the screen condenser where entrained air is removed from the fiberglass. Fiberglass is deposited from the screen condenser to a transport container.

## Claims

### Claim 1

A fiberglass recycling system for the dewatering of fiberglass that has been stripped from bobbins by liquid jets, comprising:
a) a conveyor system for transporting clusters of wetted fiberglass from an input section to a discharge section;
b) a centrifuge disposed adjacent to the discharge section of the conveyor system for receiving and dewatering the wetted fiberglass;
c) means for detecting and measuring the quantity of fiberglass clusters passing on the conveyor system and being discharged into the centrifuge; and
d) control means responsive to the detection means for controlling the speed of the centrifuge in relationship to the detected amount of fiberglass discharged from the conveyor system into the centrifuge.

### Claim 2 (depends on 1)

The fiberglass recycling system of claim 1 wherein the detecting means includes a fiber detector positioned above the conveyor surface for ascertaining the presence of fiberglass clusters and a height detector positioned adjacent to one side of the conveyor system for measuring the height of the fiberglass clusters.

### Claim 3 (depends on 2)

The fiberglass recycling system of claim 2 wherein the fiber detector and height detector are photoelectric devices.

### Claim 4 (depends on 1)

The fiberglass recycling system of claim 1 wherein the control means includes means for increasing the speed of the centrifuge to dewater the fiberglass once a predetermined volume of fiberglass has been deposited into the centrifuge.

### Claim 5 (depends on 4)

The fiberglass recycling system of claim 4 wherein the control means decreases the speed of the centrifuge after a predetermined time period sufficient to allow for the dewatering of fiberglass contained within the centrifuge.

### Claim 6 (depends on 1)

The fiberglass recycling system of claim 1 wherein the centrifuge is operable in a fill mode where the centrifuge spins at a relatively slow speed and in a dewatering mode where the centrifuge spins at a relatively fast speed; wherein the conveyor system is operable to run in a discharge mode where fiberglass is conveyed by the conveyor system and discharged into the centrifuge and an accumulation mode where at least a portion of the conveyor system conveys fiberglass toward the discharge section of the conveyor system while the discharge section does not discharge fiberglass into the centrifuge; and wherein the fiberglass recycling system further includes conveyor speed control means for maintaining the conveyor system in the discharge mode while the centrifuge is in the fill mode and for maintaining the conveyor system in the accumulation mode while the centrifuge is in the dewatering mode.

### Claim 7 (depends on 6)

The fiberglass recycling system of claim 6 wherein the input section of the conveyor system in the accumulation mode runs at a relatively slow speed compared to the speed of the conveyor system in the discharge mode.

### Claim 8 (depends on 7)

The fiberglass recycling system of claim 7 wherein the conveyor system further includes an intermediate section positioned between the input and discharge sections.

### Claim 9 (depends on 8)

The fiberglass recycling system of claim 8 wherein the intermediate section of the conveyor system in the accumulation mode runs at a relatively slow speed compared to the speed of the conveyor system in the discharge mode.

### Claim 10 (depends on 1)

The fiberglass recycling system of claim 1 further including:
a) pneumatic transport means for pneumatically transporting dewatered fiberglass from the centrifuge;
b) air removal means for removing entrained air from the dewatered fiberglass being transported by the pneumatic transport means; and
c) a transport container for collecting fiberglass from the air removal means.

### Claim 11 (depends on 10)

The fiberglass recycling system of claim 10 wherein the air removal means is a screen condenser.

### Claim 12

A fiberglass recycling system for the dewatering of fiberglass that has been stripped from bobbins by liquid jets, comprising:
a) a conveyor system for transporting clusters of fiberglass from an input section to a discharge section;
b) a centrifuge disposed adjacent the discharge section of the conveyor for receiving and dewatering the fiberglass clusters, the centrifuge having inner walls that taper outwardly from a bottom for causing fiberglass to be forced upwardly along the tapered walls as the centrifuge rotates so as to uniformly disperse the fiberglass in the centrifuge; and
c) a drive mounted to rotate said centrifuge.

### Claim 13 (depends on 12)

The fiberglass recycling system of claim 12 further including pneumatic transport means for pneumatically transporting dewatered fiberglass from the centrifuge and a screen condenser for removing entrained air from the fiberglass being transported from the centrifuge.

### Claim 14

A method of recycling fiberglass that has been stripped from bobbins by water jets, said method comprising:
a) conveying the fiberglass on a conveyor system from an input section to a discharge section;
b) depositing the fiberglass from the discharge section of the conveyor into a centrifuge;
c) detecting and measuring the quantity of fiberglass clusters passing on the conveyor system and being discharged into the centrifuge; and
d) controlling the speed of the centrifuge in relationship to the detected amount of fiberglass discharged from the conveyor system into the centrifuge.

### Claim 15 (depends on 14)

The method of claim 14 further including speeding up the centrifuge from a relatively slow speed to a relatively fast speed for a predetermined period of time sufficient to dewater the fiberglass contained within the centrifuge and then removing the dewatered fiberglass from the centrifuge.

### Claim 16 (depends on 15)

The method of claim 15 further comprising the steps of discharging the fiberglass into the centrifuge and spinning the centrifuge at a relatively slow speed until the centrifuge is filled to a selected level, and then placing the conveyor system in an accumulation mode and increasing the speed of rotation of the centrifuge while ceasing to discharge fiberglass into the centrifuge.

### Claim 17 (depends on 16)

The method of claim 16 further comprising the steps of driving the conveyor system at a relatively high speed when the same is operated in the discharge mode and driving the input section of the conveyor system at a relatively slow speed when the same is maintained in the accumulation mode.
