Method to use heat energy from black liquor
The method is for retrieving heat from black liquor wherein the black liquor is withdrawn from a digester in association with the production of cellulose pulp. The black liquor at the withdrawal stage maintains a first withdrawal temperature. At least a part of the black liquor is led to a heat exchanger. An exchange of heat takes place in the heat exchanger between the black liquor and a bleaching filtrate that has been obtained from the bleaching plant. The exchange of heat results in the bleaching filtrate experiencing a raise in temperature of at least 5° C., after which the heated bleaching filtrate is used in the bleaching plant.
1. A method to retrieve heat from black liquor, comprising:
withdrawing black liquor from a digester in association with a production of cellulose pulp,
the black liquor when withdrawn from the digester maintaining a first withdrawal temperature,
the digester maintaining a digestion temperature of 130-180° C., subsequent to withdrawal of the black liquor, reducing the first withdrawal temperature of the black liquor to a second temperature in a range of 90-125° C.,
leading at least a part of the black liquor at the second temperature to a primary heat exchanger,
exchanging heat in the primary heat exchanger between the black liquor and a bleaching filtrate that has been obtained from a bleaching plant and increasing a filtrate temperature of the bleaching filtrate to produce a heated bleaching filtrate, and
conveying the heated bleaching filtrate to the bleaching plant.
2. The method according to claim 1 , wherein the exchange of heat results in the bleaching filtrate experiencing a rise in the filtrate temperature of at least 5° C.
3. The method according to claim 1 wherein the bleaching filtrate obtained from the bleaching plant has the filtrate temperature in a range of 45-90° C. before undergoing a heat exchange with the black liquor.
4. The method according to claim 3 , wherein the withdrawn black liquor is used, before the withdrawn black liquor is led to the primary heat exchanger, in at least one stage of a digestion system, which results in the black liquor experiencing a fall in temperature of at least 20° C.
5. The method according to claim 3 , wherein a withdrawal temperature of the black liquor is reduced to a reduced temperature through a preliminary heat exchange process in a preliminary heat exchanger with a process fluid in a digestion plant, the preliminary heat exchanger being prior to the primary heat exchanger.
6. The method according to claim 3 , wherein the first withdrawal temperature of the black liquor is, prior to being led to the primary heat exchanger, reduced to a reduced temperature through at least one pressure reduction process in which steam is evaporated off from the black liquor.
7. The method according to claim 3 , wherein the first withdrawal temperature of the black liquor is reduced to a reduced temperature by using the black liquor as impregnation fluid in an impregnation stage before digestion in the digester.
8. The method according to claim 1 wherein the heated bleaching filtrate is a filtrate from a washing arrangement arranged after a pre-bleaching stage wherein the heated bleaching filtrate is used as a dilution fluid before an oxygen gas stage.
9. The method according to claim 1 wherein the first heat exchanger is arranged in association with the digester wherein the bleaching filtrate is led along lines from the bleaching plant to the primary heat exchanger and returns to the bleaching plant.
10. The method according to claim 1 wherein the primary heat exchanger is arranged in association with the bleaching plant, wherein black liquor that maintains the second temperature is led along lines from the digester to the primary heat exchanger and thereafter to an evaporation process.