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Continuous alkaline oxygen delignification of pulp, using multi reactor system with high pressure reactor part

机译:使用带有高压反应器部件的多反应器系统对纸浆进行连续的碱氧脱木质素

摘要

The reactor system includes a high pressure reactor part (R 1-R 3) in which the pulp spends a predetermined dwell time. A continuous alkaline oxygen delignification of cooked and optionally washed (W 1-W 3) cellulose pulp which has been stored in a substantially atmospheric pressure tower or pit (ST), has an average consistency of 8-16% and has a kappa value of at least 15 units (preferably greater than 20) is carried out in a multi-reactor system (R 1-R 4) by adding alkali (NaOHMAIN) to obtain an initial pH greater than 9 and by adding 5-50 kg oxygen per tonne pulp in a position upstream from the first reactor. The dwell time for the pulp in the entire reactor system is greater than 45 minutes. The pulp is pressurised to an initial pressure of more than 15 bar in a high pressure part of the system, where the necessary chemicals are added and the initial mixing is carried out, then pulp is passed through at least two reactors with mixing stations (M1-M3) in between so that the pulp pressure is at least 13 bar as it leaves the final reactor in the high pressure part. The dwell time in the reactors = t 1t 2t x, where t 1is the dwell time in the reactor before the first mixing station (M1) and x is the number of high pressure reactors.
机译:反应器系统包括高压反应器部分(R 1-R 3),其中纸浆花费预定的停留时间。已存储在基本为大气压的塔或坑(ST)中的煮熟且可选洗涤的(W 1-W 3)纤维素纸浆的连续碱性氧脱木质素,其平均稠度为8-16%,kappa值为在多反应器系统(R 1-R 4)中,通过添加碱(NaOHMAIN)以获得初始pH值大于9并通过每吨添加5-50 kg氧气,至少进行15个单元(最好大于20个单元)纸浆位于第一反应器上游的位置。纸浆在整个反应器系统中的停留时间大于45分钟。在系统的高压部分将纸浆加压至超过15 bar的初始压力,在其中添加必要的化学品并进行初始混合,然后将纸浆通过至少两个带有混合站的反应器(M1 -M3),以使纸浆压力至少为13 bar,因为它将最终反应器留在高压部分。反应器中的停留时间= t 1t 2t x,其中t 1是第一个混合站(M1)之前在反应器中的停留时间,x是高压反应器的数量。

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