Method and apparatus for controlling dryers for wood products, fabrics, paper and pulp

Claim 1

A method of drying a product to a desired final moisture content in which the product being dried moves through the dryer at an adjustable speed while being contacted by a drying medium comprising the steps of moving the product through the dryer, measuring at a location in the dryer a differential temperature, (ΔT), that relates to the difference between the temperature of the drying medium and that of the product to determine at that time and at the speed of the dryer at that time what the final moisture content of the product will be, and controlling the equilibrium value of ΔT by varying one of the components of ΔT and the speed of the product through the dryer to obtain the desired final moisture content in the product.

Claim 2

A method of drying a product to a desired final moisture content in which the product being dried moves through the dryer at an adjustable speed while being contacted by a drying medium comprising the steps of moving the product through the dryer, measuring at a location in the dryer a differential temperature, (ΔT), that relates to the difference between the temperature of the drying medium and that of the product to determine at that time and at the speed of the dryer at that time what the final moisture content of the product will be, and controlling the equilibrium value of ΔT by varying one of the components of ΔT and the speed of the product through the dryer to obtain the desired final moisture content in the product.

Claim 5

A method of drying wood products to a desired final moisture content comprising the steps of moving the wood products at a preselected speed through a dryer through which heated air is circulated, measuring the difference between the temperature of the air coming into the dryer (T i ) and the temperature of the air leaving the dryer, (T o ) and varying the temperature of the incoming air and the speed of travel of the product to obtain the desired final moisture content, continuously measuring the temperature difference between the inlet and outlet air, and continuously adjusting the temperature of the incoming air and the speed of travel of the product as required to maintain the final moisture content of the dried product within an acceptable range in accordance with the equation ##EQU6## where M=final moisture content ΔT=T i -T o , and S=speed of travel of the product through the dryer, and K 1 , K 2 , p, and q are constants for a given dryer and product.

Claim 6

A method of drying wood products to a desired final moisture content comprising the steps of moving the wood products at a preselected speed through a dryer through which heated air is circulated, measuring the difference between the temperature of the air coming into the dryer (T i ) and the temperature of the air leaving the dryer, (T o ) and varying the temperature of the incoming air and the speed of travel of the product to obtain the desired final moisture content, continuously measuring the temperature difference between the inlet and outlet air, and continuously adjusting the temperature of the incoming air and the speed of travel of the product as required to maintain the final moisture content of the dried product within an acceptable range in accordance with the equation ##EQU6## where M=final moisture content ΔT=T i -T o , and S=speed of travel of the product through the dryer, and K 1 , K 2 , p, and q are constants for a given dryer and product.

Claim 9

A method of controlling a product dryer at a temperature above that of the product to raise the temperature of the product to dry the product to a desired final moisture content in which the product being dried moves through the dryer while being contacted by a drying medium comprising the steps of moving the product through the dryer at a preselected speed, measuring the temperature of the drying medium before it contacts the product and the temperature of the drying medium after it contacts the product, at a selected location in the dryer, calculating what the final moisture content of the product will be from the equation ##EQU8## where: M 2 =the final moisture content of the product, ΔT 2 =T i -T o where T i =temperature of drying medium prior to drying pass and T o =temperature of drying medium after drying pass; S=L/Δθ where L=distance from the location of the measurement to the dryer exit, and Δθ=drying time remaining at measuring location; ##EQU9## where C 1 =a constant determined empirically for the particular product and dryer; G=mass rate of drying medium (air+H 2 O), lbs/minute; C=specific heat of drying medium, BTU/#°F.; U=Overall heat transfer coefficient As=heat transfer area of the product (both sides), sq. ft. p, K 2 and q=constants determined empirically for the particular product and dryer, and adjusting at least one of the speed of travel of the product and (ΔT) to obtain the desired final moisture content of the product.

Claim 10

A method of controlling a product dryer at a temperature above that of the product to raise the temperature of the product to dry the product to a desired final moisture content in which the product being dried moves through the dryer while being contacted by a drying medium comprising the steps of moving the product through the dryer at a preselected speed, measuring the temperature of the drying medium before it contacts the product and the temperature of the drying medium after it contacts the product, at a selected location in the dryer, calculating what the final moisture content of the product will be from the equation ##EQU8## where: M 2 =the final moisture content of the product, ΔT 2 =T i -T o where T i =temperature of drying medium prior to drying pass and T o =temperature of drying medium after drying pass; S=L/Δθ where L=distance from the location of the measurement to the dryer exit, and Δθ=drying time remaining at measuring location; ##EQU9## where C 1 =a constant determined empirically for the particular product and dryer; G=mass rate of drying medium (air+H 2 O), lbs/minute; C=specific heat of drying medium, BTU/#°F.; U=Overall heat transfer coefficient As=heat transfer area of the product (both sides), sq. ft. p, K 2 and q=constants determined empirically for the particular product and dryer, and adjusting at least one of the speed of travel of the product and (ΔT) to obtain the desired final moisture content of the product.

Claim 11

A method of drying a product to a desired final moisture content in which the product being dried moves through the dryer at an adjustable speed (S) while being contacted by a drying medium comprising the steps of moving the product through the dryer, measuring at a location in the dryer a differential temperature, (ΔT), that relates to the difference between the temperature of the drying medium and that of the product, calculating what the final moisture content (M) of the product will be using the equation M=ΔT-1/S and controlling at least one of the value of (ΔT) or the speed of the product through the dryer to obtain the desired moisture content in the product.

Claim 12

A method of drying a product to a desired final moisture content in which the product being dried moves through the dryer at an adjustable speed (S) while being contacted by a drying medium comprising the steps of moving the product through the dryer, measuring at a location in the dryer a differential temperature, (ΔT), that relates to the difference between the temperature of the drying medium and that of the product, calculating what the final moisture content (M) of the product will be using the equation M=ΔT-1/S and controlling at least one of the value of (ΔT) or the speed of the product through the dryer to obtain the desired moisture content in the product.

Claim 15

A method of drying products such as wood to a final moisture content within an acceptable range comprising the steps of moving the products at a preselected speed (S) through a dryer in which heated air is circulated, continuously measuring the difference between the temperature of the air before it contacts the product (T i ) and the temperature of the air after it has contacted the product, (T o ) continuously calculating what the final moisture content (M) will be using the equation M=ΔT-1/S and continuously adjusting the temperature of the incoming air and the speed of travel of the product as required for the final moisture content of the dried product to be within the acceptable range.

Claim 16

A method of drying products such as wood to a final moisture content within an acceptable range comprising the steps of moving the products at a preselected speed (S) through a dryer in which heated air is circulated, continuously measuring the difference between the temperature of the air before it contacts the product (T i ) and the temperature of the air after it has contacted the product, (T o ) continuously calculating what the final moisture content (M) will be using the equation M=ΔT-1/S and continuously adjusting the temperature of the incoming air and the speed of travel of the product as required for the final moisture content of the dried product to be within the acceptable range.