Process of producing pulp, for manufacture of fiberboard, in a closed backwater system

Claim 2

In a process for manufacturing fiberboard according to the wet method and with a closed backwater system which includes in sequence the steps of: defibrating lignocellulose fiber containing chips within a disintegrating apparatus in a vapor phase of saturated steam of superatmospheric pressure, suspending the defibrated material discharged from the defibrating step in backwater serving as propellant liquid to form a pulp suspension, forming wet sheets from the pulp suspension, mechanically separating off water from the wet sheets and recycling the water as backwater to form a new pulp suspension and drying the sheets of evaporation of water, the improvement comprising the steps of liberating steam from the defibrated material and preheating the chips at atmospheric pressure with said liberated steam, then de-watering the steam-heated chips to a dry content of at least 50 percent, thereafter feeding the thus heated and de-watered chips to the defibrating step and simultaneously supplying backwater separated from the wet sheets to the defibration step for minimizing overheating of the fiber material.

Claim 3

An improved process as claimed in claim 1, wherein the preheated chips are de-watered by mechanically compressing the chips.

Claim 4

An improved process as claimed in claim 2, including the further step of partially drying the compressed chips before they are fed into the defibrating step.

Claim 5

An improved process as claimed in claim 1, wherein the chips are preheated to a temperature in the range from 90° to 100° C.

Claim 6

An improved process as claimed in claim 1, further including the step of discharging the steam liberated from the defibrated material discharged in the defibrating step under a steam pressure sufficient to force it through a layer of chips to be preheated.

Claim 7

In a process for manufacturing fiberboard according to the wet method and with a closed backwater system which includes in sequence the steps of: defibrating lignocellulose fiber containing chips within a disintegrating apparatus in an atmosphere or saturated steam, suspending the defibrated material discharged from the defibrating step in backwater serving as propellant liquid to form a pulp suspension, forming wet sheets from the pulp suspension, mechanically separating off water from the wet sheets and recycling the water as backwater to form a new pulp suspension and drying the sheets by evaporation of water, the improvement comprising the steps of liberating steam from the defibrated material and preheating the chips with said steam to a temperature in the range of 90° to 100° C, then de-watering the steam-heated chips to a dry content of at least 50 percent, thereafter feeding the thus heated and de-watered chips to the defibrating step and simultaneously supplying backwater separated from the wet sheets to the defibration step for minimizing overheating of the fiber material.

Claim 8

In a process for manufacturing fiberboard according to the wet method and with a closed backwater system which includes in sequence the steps of: defibrating lignocellulose fiber containing chips within a disintegrating apparatus in an atmosphere or saturated steam, suspending the defibrated material discharged from the defibrating step in backwater serving as propellant liquid to form a pulp suspension, forming wet sheets from the pulp suspension, mechanically separating off water from the wet sheets and recycling the water as backwater to form a new pulp suspension and drying the sheets by evaporation of water, the improvement comprising the steps of liberating steam from the defibrated material and preheating the chips with said steam to a temperature in the range of 90° to 100° C, then de-watering the steam-heated chips to a dry content of at least 50 percent, thereafter feeding the thus heated and de-watered chips to the defibrating step and simultaneously supplying backwater separated from the wet sheets to the defibration step for minimizing overheating of the fiber material.

Claim 9

An improved process according to claim 6, further including the step of blowing at least a portion of the liberated steam of atmospheric pressure through a layer of chips to be preheated.

Claim 10

An improved process according to claim 6, further including the step of discharging the steam liberated from the defibrated material discharged in the defibrating step under a steam pressure sufficient to force it through a layer of chips to be preheated.

Claim 11

In an improved process for manufacturing fiberboard according to the wet method and with a closed backwater system which includes in sequence the steps of: defibrating lignocellulose fiber containing chips within a disintegrating apparatus in a vapor phase of saturated steam of super-atmospheric pressure, suspending the defibrated material discharged from the defibrating step in backwater serving as propellant liquid to form a pulp suspension, forming wet sheets from the pulp suspension, mechanically separating off water from the wet sheets and recycling the water as backwater to form a new pulp suspension and drying the sheets by evaporation of water, the improvement comprising the steps of preheating the chips with steam, then dewatering the heated chips by mechanical compression thereof to a dry content of at least 50 percent, thereafter feeding the thus heated and de-watered chips to the defibrating step and simultaneously supplying backwater separated from the wet sheets to the defibration step for mimimizing overheating of the fiber material and returning at least partially the water removed by the mechanical compression to the process for washing the chips.

Claim 12

In an improved process for manufacturing fiberboard according to the wet method and with a closed backwater system which includes in sequence the steps of: defibrating lignocellulose fiber containing chips within a disintegrating apparatus in a vapor phase of saturated steam of super-atmospheric pressure, suspending the defibrated material discharged from the defibrating step in backwater serving as propellant liquid to form a pulp suspension, forming wet sheets from the pulp suspension, mechanically separating off water from the wet sheets and recycling the water as backwater to form a new pulp suspension and drying the sheets by evaporation of water, the improvement comprising the steps of preheating the chips with steam, then dewatering the heated chips by mechanical compression thereof to a dry content of at least 50 percent, thereafter feeding the thus heated and de-watered chips to the defibrating step and simultaneously supplying backwater separated from the wet sheets to the defibration step for mimimizing overheating of the fiber material and returning at least partially the water removed by the mechanical compression to the process for washing the chips.

Claim 13

An improved process as claimed in claim 9, wherein the backwater supplied to the defibrating step is preheated to a temperature between 100° and 170° C.

Claim 14

An improved process according to claim 9, in which the water removed by mechanical compression is also used as spray water in the wet forming step.