Method of controlling a mobile pugmill having a weight metering control system

• US 6,036,353 A
• Filed: 02/16/1999
• Issued: 03/14/2000
• Est. Priority Date: 01/29/1996
• Status: Expired due to Fees

• Current Assignee: Excel Machinery Company Incorporated
• Original Assignee: Excel Machinery Company Incorporated
• Inventors: Paetzold, John
• Primary Examiner(s): Cooley, Charles E.
• Application Number:
  US09/250,961
• Time in Patent Office: 392 Days
• Field of Search: 366/1, 366/2, 366/6, 366/8, 366/16-18, 366/20, 366/27-29, 366/33-35, 366/37, 366/38, 366/40, 366/50, 366/141, 366/151.1, 366/152.1, 366/186, 366/606
• US Class Current: 366/8
• CPC Class Codes: B01F 23/565 by introducing liquids in solid material, e.g. to obtain slurries
• CPC Class Codes: B01F 23/60 Mixing solids with solids
• CPC Class Codes: B01F 33/502 Vehicle-mounted mixing devices
• CPC Class Codes: B01F 35/832 Flow control by weighing
• CPC Class Codes: B01F 35/881 by weighing, e.g. with automatic discharge
• CPC Class Codes: B01F 35/892 for solid materials, e.g. using belts, vibrations, hoppers with variable outlets or hoppers with rotating elements, e.g. screws, at their outlet B01F35/82 - B01F35/88 take precedence

Abstract

A portable chassis-mounted continuous flow, blending and mixing plant utilizing a Programmable Logic Controller and belt scales to continuously meter and adjust the flow of aggregate as well as maintain the proper ratio and flow of additives, both dry and liquid.

Claims

1. A method of controlling a blending and mixing plant comprising the steps of:

a) providing an ideal aggregate flow rate;

b) providing an ideal additive percentage set point;

c) sending the ideal aggregate flow rate to an aggregate process controller;

d) receiving a current aggregate flow rate signal from an aggregate sensor;

e) comparing the ideal aggregate flow rate to the current aggregate flow rate in the aggregate process controller;

f) calculating the ideal additive flow rate from the additive percentage set point and the current aggregate flow rate;

g) changing the current aggregate flow rate by sending an aggregate output signal from the aggregate process controller to an aggregate dispenser;

h) sending the ideal additive flow rate to an additive process controller;

i) receiving a current additive flow rate signal from an additive sensor;

j) comparing the ideal additive flow rate to the current additive flow rate in the additive process controller;

k) changing the current additive flow rate by sending an output signal from the additive process controller to an additive dispenser; and

l) repeating steps c-k at predetermined intervals.

2. The method of controlling a blending and mixing plant in claim 1 wherein the additive is a dry additive.

3. The method of controlling a blending and mixing plant in claim 2 wherein the additive sensor is a belt scale sensor.

4. The method of controlling a blending and mixing plant in claim 2 wherein the additive process controller is a proportional integral derivative controller.

5. The method of controlling a blending and mixing plant in claim 1 wherein the additive is a liquid additive.

6. The method of controlling a blending and mixing plant in claim 5 wherein the additive sensor is a flow meter.

7. The method of controlling a blending and mixing plant in claim 5 wherein the additive process controller is a proportional controller.

8. The method of controlling a blending and mixing plant in claim 1 wherein the aggregate process controller is a proportional integral derivative controller.

9. The method of controlling a blending and mixing plant in claim 1 wherein the aggregate sensor is a belt scale sensor.