CA2043605C - Process for the partial combustion of cellulose spent liquors - Google Patents
Process for the partial combustion of cellulose spent liquors Download PDFInfo
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- CA2043605C CA2043605C CA002043605A CA2043605A CA2043605C CA 2043605 C CA2043605 C CA 2043605C CA 002043605 A CA002043605 A CA 002043605A CA 2043605 A CA2043605 A CA 2043605A CA 2043605 C CA2043605 C CA 2043605C
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- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21C—PRODUCTION OF CELLULOSE BY REMOVING NON-CELLULOSE SUBSTANCES FROM CELLULOSE-CONTAINING MATERIALS; REGENERATION OF PULPING LIQUORS; APPARATUS THEREFOR
- D21C11/00—Regeneration of pulp liquors or effluent waste waters
- D21C11/12—Combustion of pulp liquors
- D21C11/125—Decomposition of the pulp liquors in reducing atmosphere or in the absence of oxidants, i.e. gasification or pyrolysis
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23C—METHODS OR APPARATUS FOR COMBUSTION USING FLUID FUEL OR SOLID FUEL SUSPENDED IN A CARRIER GAS OR AIR
- F23C5/00—Disposition of burners with respect to the combustion chamber or to one another; Mounting of burners in combustion apparatus
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- Chemical & Material Sciences (AREA)
- Combustion & Propulsion (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Paper (AREA)
- Polysaccharides And Polysaccharide Derivatives (AREA)
- Regulation And Control Of Combustion (AREA)
- Breeding Of Plants And Reproduction By Means Of Culturing (AREA)
- Pyrane Compounds (AREA)
- Medicines Containing Plant Substances (AREA)
- Gasification And Melting Of Waste (AREA)
- Solid Fuels And Fuel-Associated Substances (AREA)
Abstract
The present invention relates to a process for partial combus-tion of cellulose spent liquors using a burner connected to a reactor while adding an oxygen containing gas, maintaining a temperature of more than 700°C within the reactor and that at least half of the non-fuel related amount of oxygen which shall be added to the reactor to partially combust the cellulose spent liquor added through the burner, is added to the reactor as a hot oxygen containing gas added through a channel arranged coaxially around a liquor lance provided for the addition of said cellulose spent liquor, whereby the weight ratio between the oxygen of the oxygen containing gas and the cellulose spent liquor solids is in the range of 0.1-0.7:1.
Description
~~~360 PROCESS FOR THE PARTIAL COMBUSTION OF CELLULOSE SPENT LIQUOR
nrcrororrnr,i Technical field The present invention relates to a process for partial combus-tion of cellulose spent liquors from the cellulose industry in a burner connected to a reactor, which burner comprises a cen-trally arranged burner gun or liquor Lance equipped with a noz-zle at its front end which adds liquor and, a coaxially ar-ranged tubular channel around the liquor lance, in which chan-nel an oxygen containing gas is added to support partial com-bustion, whereby the oxygen containing gas, prior to entry in the coaxially arranged channel, has been given a vortex move-ment.
The object of the present invention is to facilitate partial combustion of the cellulose spent liquor through use of a burner creating a stable, self-igniting flame at low air/fuel ratios.
Background of the invention The cellulose industry generates spent liquors differing in composition according to the delignification process used.
Within the sulphate pulping industry, spent Liquor, commonly referred to as black liquor, contains valuable chemicals and energy in the form of combustible carbonaceous compounds. At the present time these chemicals and energy are normally recov-ered in a re-covery boiler in which the black Liquor is com-pletely burned.
Partial combustion of black Liquor in a gasification reactor as in the present invention generates a combustible gas comprising H2, C0, CO2, and droplets of molten inorganic chemicals.
In conjunction with pulp bleaching, a diluted liquor comprising organic matter and sodium salts is obtained. Mechanical and semi-chemical pulping processes also generate diluted liquors of different compositions. These as well as other waste and ~;~~~~0 spent liquors generated in the cellulose industry can, after concentration be used as a feedstock in the process of the pre-sent invention.
Although the following description describes the present inven-tion as it applies to black liquor it is not restricted only to this particular liquor in its application.
The mechanisms related to partial combustion of black liquor are fairly well understood and are applied inter alia in the lower part of the soda recovery boiler. The difference between the present burner and a liquor burner in a soda recovery boiler is, however, great inter alia due to the low degree of Liquor atomization in recovery boiler burners and the absence of a well-defined liquor flame.
A major difference between the burner of the present invention and conventional oil burners is that a stable flame has to be formed with the use of a considerably lower amount of air or oxygen carrier.
As the exemplification below show black Liquor as a fuel is characterized by a relatively low calorific value and high wa-ter and ash contents.
Calorific value of the dry substance 13 GJ/ton dry substance (DS) Elementary composition C29H34~20Na9S2 Dry solids content 65 viscosity at 100°C 100 cSt.
The presence of sodium compounds in the black liquor and its inherently high oxygen content make it a very reactive fuel, which means, provided an adequate burner design is at hand that the carbon conversion already in the flame zone becomes high, in spite of the fact that the combustion is substoichiometric.
nrcrororrnr,i Technical field The present invention relates to a process for partial combus-tion of cellulose spent liquors from the cellulose industry in a burner connected to a reactor, which burner comprises a cen-trally arranged burner gun or liquor Lance equipped with a noz-zle at its front end which adds liquor and, a coaxially ar-ranged tubular channel around the liquor lance, in which chan-nel an oxygen containing gas is added to support partial com-bustion, whereby the oxygen containing gas, prior to entry in the coaxially arranged channel, has been given a vortex move-ment.
The object of the present invention is to facilitate partial combustion of the cellulose spent liquor through use of a burner creating a stable, self-igniting flame at low air/fuel ratios.
Background of the invention The cellulose industry generates spent liquors differing in composition according to the delignification process used.
Within the sulphate pulping industry, spent Liquor, commonly referred to as black liquor, contains valuable chemicals and energy in the form of combustible carbonaceous compounds. At the present time these chemicals and energy are normally recov-ered in a re-covery boiler in which the black Liquor is com-pletely burned.
Partial combustion of black Liquor in a gasification reactor as in the present invention generates a combustible gas comprising H2, C0, CO2, and droplets of molten inorganic chemicals.
In conjunction with pulp bleaching, a diluted liquor comprising organic matter and sodium salts is obtained. Mechanical and semi-chemical pulping processes also generate diluted liquors of different compositions. These as well as other waste and ~;~~~~0 spent liquors generated in the cellulose industry can, after concentration be used as a feedstock in the process of the pre-sent invention.
Although the following description describes the present inven-tion as it applies to black liquor it is not restricted only to this particular liquor in its application.
The mechanisms related to partial combustion of black liquor are fairly well understood and are applied inter alia in the lower part of the soda recovery boiler. The difference between the present burner and a liquor burner in a soda recovery boiler is, however, great inter alia due to the low degree of Liquor atomization in recovery boiler burners and the absence of a well-defined liquor flame.
A major difference between the burner of the present invention and conventional oil burners is that a stable flame has to be formed with the use of a considerably lower amount of air or oxygen carrier.
As the exemplification below show black Liquor as a fuel is characterized by a relatively low calorific value and high wa-ter and ash contents.
Calorific value of the dry substance 13 GJ/ton dry substance (DS) Elementary composition C29H34~20Na9S2 Dry solids content 65 viscosity at 100°C 100 cSt.
The presence of sodium compounds in the black liquor and its inherently high oxygen content make it a very reactive fuel, which means, provided an adequate burner design is at hand that the carbon conversion already in the flame zone becomes high, in spite of the fact that the combustion is substoichiometric.
~C ~ ~ ~ ~ s, The vortex burner described in the present invention provides high combustion efficiency and flame stability using black liq-uor as fuel in a relatively small reactor volume. The tempera' lure in the reactor is above 700°C, preferably around 900°C.
The molten inorganic chemicals, substantially sodium carbonate and sodium sulphide, are separated from the process gas in a quench dissolver connected to the reactor. The process gas is substantially composed of carbon monoxide, carbon dioxide, and hydrogen. The volume ratios of carbon monoxide, and carbon di-oxide, in the process gas is allowed to vary between 0.8:1, and 1.8:1, and is controlled by i.a. the amount of oxygen added.
The flow pattern near the burner is influenced to a great ex-tent by the level of vortex which can be controlled by e.g. ad-jesting the vortex btading. The radial flow rate of the oxygen containing gas is thereby markedly affected with a maintained axial flow rate. The main principle of the vortex burner is to recircutate a portion of the gases through an internal recirculation zone towards the Liquor lance. This internal recirculation zone facilitates combustion and stabilizes the flame and the recirculated hot gases add energy for ignition of the Liquor spray. The internal recirculation zone also serves as a depot for heat and reactive gas components.
The mixing of the liquor spray and the combustion air is sup-ported by the turbulent shear surface between the recircutation zone and the discharged gas and liquor droplets.
An outer recirculation zone, however, of less importance for the stability of the flame is also developed. Its shape is in-fluenced more by the geometry of the reactor than by the geome-try of the burner.
The degree of atomization of the liquor is of great importance for obtaining a stable black liquor (tame, the extension of the flame and the high carbon conversion. The Theological proper-ties of the black liquor are of significant importance to the 3 _ 27243-5~'~~~~~~'~
degree of atomization which can be achieved in a given nozzle.
The viscosity of the black liquor can be influenced by e.g.
heating and/or the addition of additives and normally the black liquor is being heated to above 100°C for use in the present invention. The viscosity of the black liquor at the moment of atomization should preferably be below 200 cSt, more preferably less than 100 cSt.
Atomization of the black liquor can be further enhanced by flashing the liquor into the reactor in which case the liquor is preheated to a temperature above its boiling point at the operating pressure of the reactor.
Several types of atomizing nozzles are available but only a few varieties are suitable for atomizing cellulose spent liquors, such as black liquor, in the present invention.
"Twin-fluid" nozzles are most suitable for use in the present burner. A common feature of '°twin-fluid" nozzles is that a relatively high gas flow rate is necessary for the supply of energy for the atomization. Another important feature of these nozzles is that the resulting size of th.e droplets decrease with increasing density of the atomizing gas. Depending on how the two fluid phases are brought together several mechanisms for forming droplets, such as shearing between ligaments, combination and formation of spheres of liquor droplets and high turbulence decomposition of the liquor spray can be anticipated.
Description of the Present Tn~ention The present invention describes a process for efficient substoichiometric combustion of cellulose spent liquors, using a burner connected to a reactor, which invention is characterized _ 4 _ 27243-55 ~' ~ ~ ~ ~' in that at least half of the non-fuel related amount of oxygen which shall be added to the reactor to partially burn the black liquor added through the burner, is added to the reactor in the form of a hot oxygen containing gas which gas is added through a tubular channel arranged coaxially around a liquor lance arranged for the addition of said cellulose spent liquor, the weight ratio between the amount of oxygen of the oxygen containing gas added through the burner and of the added cellulose spent liquor solids being in the range of 0.1°0.7:1, preferably 0.15-0.5:1.
In preferred embodiments: the stream of liquor in the liquor lance is brought into contact with a gas having a high velocity and a higher pressure than said cellulose spent liquor, increasing the velocity of the stream of liquor which forms a finely dispersed divergent spray of cellulose spent liquor exiting from 'the lower part of said liquor lance; the cellulose spent liquor is discharged from the lower part of said liquor lance through at least three symmetrically arranged orifices or through a circular gap; the oxygen containing gas is passed through a diverging nozzle arranged coaxially around the liquor lance, which nozzle ends in the reaction zone of said reactor;
and the vortex blading is arranged substantially behind the atomizing nozzle of the liquor lance.
The attached drawing shows a vortex burner and two different "twin-fluid" nozzles, whereby FIG. 1 schematically shows a vortex burner with its recirculation zone;
FIG. 2 shows an embodiment of a "twin-fluid'° nozzle in an axial cross-section;
FIG. 3 shows a front view of the nozzle according to FIG. 2 seen along the line III-III of FIG. 2;
FIG. 4 shows a second embodiment of a "twin-fluid"
nozzle in axial cross-section; and FIG. 5 shows a front view of the nozzle according to FIG. 4 seen along the line V-V of FIG. 4.
FIG. 1 schematically shows a vortex burner 1 placed in a combustion chamber 22, and a vortex generator 24 arranged in a channel 23 for the purpose of adding air. The unbroken line in FIG. 1 shows the spatial distribution of the internal recircula-tion, the dotted line,the internal recirculation zone, and the dashed line shows the limit of the return flow, i.e., the limit along which the recirculation turns (the axial zero-velocity line). The dashed line in the lower part of FIG. 1 also shows the limits of the outer recirculation. The vortex generator 24 is placed substantially behind the lower part of the liquor lance which means that the combustion air added outside the nozzle will circulate around the liquor lance before it meets and carries the atomized black liquor. By arranging the vortex generator adequately a flame having a toraidal vortex is developed, an important advantage for the stability of the flame and the course of the partial combustion.
FIGS. 2 and 3 show a twin-fluid nozzle where the liquor and gas are mixed and then forced under high pressure through several symmetrically arranged circular openings 3. These openings are the ends of so-called Y-jet atomizing nozzles comprised of two tubes 4 and 5, the former in contact with an outer tube 6 for the purpose of adding black liquor and the latter in contact with an >~3~0~~
inner concentric annular tube 7 for the purpose of adding atomiz-ing gas, such as air or steam. The openings 3 diverge producing divergent atomized jets from the lower part 2 of the liquor lance 1. A hood 9 fitted to the body 10 of the liquor lance, holds the Y-jet atomizer 8 in place. The body 10 encloses the concentric annular tubes 6 and 7. The black liquor is introduced into the liquor lance 1 through an inlet tube 20 and the air through another inlet tube 21.
FIGS. 4 and 5 show an embodiment of the burner gun having three concentric annular tubes 11, 12, and 13. Air is fed through the outer and the inner tubes ll, and 13, while black liquor is fed through the intermediate tube 12. The air is divided through the 18 symmetrically distributed holes 14, and 15 shown in the figures, while black liquor is forced through an annular gap 16. The holes 14 are hereby obliquely directed in one direction and the holes 15 obliquely directed in the opposite direction. The black liquor is fed through the gap 16 and meets a lip 17 forcing it in an inward direction. Now in the form of a film the black liquor is met by the air coming through the holes 16 and is atomized. This initial air-black liquor mixture is met by additional air outside the lip 17, creating a diverging jet of finely dispersed black liquor. The black liquor is added to the burner through an inlet tube 20 and the air through two inlet tubes 21.
Although air has been used in the description above the invention is not restricted to air but other gases, such as steam, nitrogen or oxygen enriched air can be used as atomizing gas.
- 6a -~:~4 i~~~
When designing burners great attention has to be paid to the weight relationship between the air and fuel added.
The black liquor described herein is a fuel possessing unusual properties and thus a burner which shall provide a stable flame - ~b -must be designed accordingly.
Different fuels contain different amounts of chemically bound oxygen. Bitumenous coal usually contains between 4-10 % of bound oxygen. Fuel oils contain less than 1 % of bound oxygen.
Black liquor dry solids contains about 35 % by weight of bound oxygen calculated on dry matter. This affects the design of burners for combustion of black liquor since only a small amount of oxygen, air or oxygen enriched air can be added to the burner to obtain the desired level of combustion.
The air/fuel ratio (by weight) for some fuels at stoichiometric combustion are exemplified below:
Antracite Air/fuel 10-12:1 Ethyl alcohol "- 9:1 Black liquor "- 4-5:1 Diesel oil/heavy oil "- 13-15:1 A burner for partial combustion of black liquor in accordance with the present invention is designed for an air/fuel solids ratio in the order of 0.5-3:1 which thus is considerably lower than ratios applied at stoichiometric as well as substoichiometric combustion of most other fuels. Since air consists of about 23 % by weight of oxygen the present black Liquor burner is thus designed for an oxygen added/black liquor solids added ratio in the range of 0.1-0.7:1. To compensate for the low air/fuel ratios and to achieve reasonable gas veloci-ties the air should be preheated to at least 100°C, preferably to 300oC and it should further be given vortex movement.
Preheating of the air adds energy in close proximity of the burner, which further supports the stability of the flame. The larger part of the oxygen required for the partial combustion is added through a channel arranged coaxially around the liquor lance which channel in turn ends in the reactor in a divergent burner tile. Part of the oxygen required for the partial com-_ 7 _ ~~~~~U=~
bustion can be added to the flame zone through the atomizing nozzle and optionally, another part can be added through secon-dary air gates in the upper part of the reactor.
8 _ :e
The molten inorganic chemicals, substantially sodium carbonate and sodium sulphide, are separated from the process gas in a quench dissolver connected to the reactor. The process gas is substantially composed of carbon monoxide, carbon dioxide, and hydrogen. The volume ratios of carbon monoxide, and carbon di-oxide, in the process gas is allowed to vary between 0.8:1, and 1.8:1, and is controlled by i.a. the amount of oxygen added.
The flow pattern near the burner is influenced to a great ex-tent by the level of vortex which can be controlled by e.g. ad-jesting the vortex btading. The radial flow rate of the oxygen containing gas is thereby markedly affected with a maintained axial flow rate. The main principle of the vortex burner is to recircutate a portion of the gases through an internal recirculation zone towards the Liquor lance. This internal recirculation zone facilitates combustion and stabilizes the flame and the recirculated hot gases add energy for ignition of the Liquor spray. The internal recirculation zone also serves as a depot for heat and reactive gas components.
The mixing of the liquor spray and the combustion air is sup-ported by the turbulent shear surface between the recircutation zone and the discharged gas and liquor droplets.
An outer recirculation zone, however, of less importance for the stability of the flame is also developed. Its shape is in-fluenced more by the geometry of the reactor than by the geome-try of the burner.
The degree of atomization of the liquor is of great importance for obtaining a stable black liquor (tame, the extension of the flame and the high carbon conversion. The Theological proper-ties of the black liquor are of significant importance to the 3 _ 27243-5~'~~~~~~'~
degree of atomization which can be achieved in a given nozzle.
The viscosity of the black liquor can be influenced by e.g.
heating and/or the addition of additives and normally the black liquor is being heated to above 100°C for use in the present invention. The viscosity of the black liquor at the moment of atomization should preferably be below 200 cSt, more preferably less than 100 cSt.
Atomization of the black liquor can be further enhanced by flashing the liquor into the reactor in which case the liquor is preheated to a temperature above its boiling point at the operating pressure of the reactor.
Several types of atomizing nozzles are available but only a few varieties are suitable for atomizing cellulose spent liquors, such as black liquor, in the present invention.
"Twin-fluid" nozzles are most suitable for use in the present burner. A common feature of '°twin-fluid" nozzles is that a relatively high gas flow rate is necessary for the supply of energy for the atomization. Another important feature of these nozzles is that the resulting size of th.e droplets decrease with increasing density of the atomizing gas. Depending on how the two fluid phases are brought together several mechanisms for forming droplets, such as shearing between ligaments, combination and formation of spheres of liquor droplets and high turbulence decomposition of the liquor spray can be anticipated.
Description of the Present Tn~ention The present invention describes a process for efficient substoichiometric combustion of cellulose spent liquors, using a burner connected to a reactor, which invention is characterized _ 4 _ 27243-55 ~' ~ ~ ~ ~' in that at least half of the non-fuel related amount of oxygen which shall be added to the reactor to partially burn the black liquor added through the burner, is added to the reactor in the form of a hot oxygen containing gas which gas is added through a tubular channel arranged coaxially around a liquor lance arranged for the addition of said cellulose spent liquor, the weight ratio between the amount of oxygen of the oxygen containing gas added through the burner and of the added cellulose spent liquor solids being in the range of 0.1°0.7:1, preferably 0.15-0.5:1.
In preferred embodiments: the stream of liquor in the liquor lance is brought into contact with a gas having a high velocity and a higher pressure than said cellulose spent liquor, increasing the velocity of the stream of liquor which forms a finely dispersed divergent spray of cellulose spent liquor exiting from 'the lower part of said liquor lance; the cellulose spent liquor is discharged from the lower part of said liquor lance through at least three symmetrically arranged orifices or through a circular gap; the oxygen containing gas is passed through a diverging nozzle arranged coaxially around the liquor lance, which nozzle ends in the reaction zone of said reactor;
and the vortex blading is arranged substantially behind the atomizing nozzle of the liquor lance.
The attached drawing shows a vortex burner and two different "twin-fluid" nozzles, whereby FIG. 1 schematically shows a vortex burner with its recirculation zone;
FIG. 2 shows an embodiment of a "twin-fluid'° nozzle in an axial cross-section;
FIG. 3 shows a front view of the nozzle according to FIG. 2 seen along the line III-III of FIG. 2;
FIG. 4 shows a second embodiment of a "twin-fluid"
nozzle in axial cross-section; and FIG. 5 shows a front view of the nozzle according to FIG. 4 seen along the line V-V of FIG. 4.
FIG. 1 schematically shows a vortex burner 1 placed in a combustion chamber 22, and a vortex generator 24 arranged in a channel 23 for the purpose of adding air. The unbroken line in FIG. 1 shows the spatial distribution of the internal recircula-tion, the dotted line,the internal recirculation zone, and the dashed line shows the limit of the return flow, i.e., the limit along which the recirculation turns (the axial zero-velocity line). The dashed line in the lower part of FIG. 1 also shows the limits of the outer recirculation. The vortex generator 24 is placed substantially behind the lower part of the liquor lance which means that the combustion air added outside the nozzle will circulate around the liquor lance before it meets and carries the atomized black liquor. By arranging the vortex generator adequately a flame having a toraidal vortex is developed, an important advantage for the stability of the flame and the course of the partial combustion.
FIGS. 2 and 3 show a twin-fluid nozzle where the liquor and gas are mixed and then forced under high pressure through several symmetrically arranged circular openings 3. These openings are the ends of so-called Y-jet atomizing nozzles comprised of two tubes 4 and 5, the former in contact with an outer tube 6 for the purpose of adding black liquor and the latter in contact with an >~3~0~~
inner concentric annular tube 7 for the purpose of adding atomiz-ing gas, such as air or steam. The openings 3 diverge producing divergent atomized jets from the lower part 2 of the liquor lance 1. A hood 9 fitted to the body 10 of the liquor lance, holds the Y-jet atomizer 8 in place. The body 10 encloses the concentric annular tubes 6 and 7. The black liquor is introduced into the liquor lance 1 through an inlet tube 20 and the air through another inlet tube 21.
FIGS. 4 and 5 show an embodiment of the burner gun having three concentric annular tubes 11, 12, and 13. Air is fed through the outer and the inner tubes ll, and 13, while black liquor is fed through the intermediate tube 12. The air is divided through the 18 symmetrically distributed holes 14, and 15 shown in the figures, while black liquor is forced through an annular gap 16. The holes 14 are hereby obliquely directed in one direction and the holes 15 obliquely directed in the opposite direction. The black liquor is fed through the gap 16 and meets a lip 17 forcing it in an inward direction. Now in the form of a film the black liquor is met by the air coming through the holes 16 and is atomized. This initial air-black liquor mixture is met by additional air outside the lip 17, creating a diverging jet of finely dispersed black liquor. The black liquor is added to the burner through an inlet tube 20 and the air through two inlet tubes 21.
Although air has been used in the description above the invention is not restricted to air but other gases, such as steam, nitrogen or oxygen enriched air can be used as atomizing gas.
- 6a -~:~4 i~~~
When designing burners great attention has to be paid to the weight relationship between the air and fuel added.
The black liquor described herein is a fuel possessing unusual properties and thus a burner which shall provide a stable flame - ~b -must be designed accordingly.
Different fuels contain different amounts of chemically bound oxygen. Bitumenous coal usually contains between 4-10 % of bound oxygen. Fuel oils contain less than 1 % of bound oxygen.
Black liquor dry solids contains about 35 % by weight of bound oxygen calculated on dry matter. This affects the design of burners for combustion of black liquor since only a small amount of oxygen, air or oxygen enriched air can be added to the burner to obtain the desired level of combustion.
The air/fuel ratio (by weight) for some fuels at stoichiometric combustion are exemplified below:
Antracite Air/fuel 10-12:1 Ethyl alcohol "- 9:1 Black liquor "- 4-5:1 Diesel oil/heavy oil "- 13-15:1 A burner for partial combustion of black liquor in accordance with the present invention is designed for an air/fuel solids ratio in the order of 0.5-3:1 which thus is considerably lower than ratios applied at stoichiometric as well as substoichiometric combustion of most other fuels. Since air consists of about 23 % by weight of oxygen the present black Liquor burner is thus designed for an oxygen added/black liquor solids added ratio in the range of 0.1-0.7:1. To compensate for the low air/fuel ratios and to achieve reasonable gas veloci-ties the air should be preheated to at least 100°C, preferably to 300oC and it should further be given vortex movement.
Preheating of the air adds energy in close proximity of the burner, which further supports the stability of the flame. The larger part of the oxygen required for the partial combustion is added through a channel arranged coaxially around the liquor lance which channel in turn ends in the reactor in a divergent burner tile. Part of the oxygen required for the partial com-_ 7 _ ~~~~~U=~
bustion can be added to the flame zone through the atomizing nozzle and optionally, another part can be added through secon-dary air gates in the upper part of the reactor.
8 _ :e
Claims (14)
1. A process for partial combustion of a cellulose spent liquor which comprises burning the spent liquor in a burner connected to a reactor while adding an oxygen containing gas, wherein a temperature of more than 700°C is maintained within the reactor and at least half of the non-fuel related amount of oxygen which shall be added to the reactor to partially combust the cellulose spent liquor added through the burner, is added to the reactor as a hot oxygen containing gas added through a channel arranged coaxially around a liquor lance provided for the addition of said cellulose spent liquor, whereby the weight ratio between the oxygen of the oxygen containing gas and the cellulose spent liquor solids is in the range of 0.1-0.7:1.
2. A process according to claim 1, wherein the weight ratio between oxygen added in the oxygen containing gas and the cellulose spent liquor solids is 0.15-0.5:1.
3. A process according to claim 1, wherein the oxygen containing gas added through the coaxial channel has a vortex movement.
4. A process according to claim 1, wherein the oxygen containing gas added through the coaxial channel is forced to pass through vortex blading.
5. A process according to claim 1, wherein the stream of liquor in the liquor lance is brought into contact with a gas having a high velocity and a higher pressure than said cellulose spent liquor, increasing the velocity of the stream of liquor which forms a finely dispersed divergent spray of cellulose spent liquor exiting from the lower part of said liquor lance.
6. A process according to any one of claims 1 to 5, wherein the cellulose spent liquor is discharged from the lower part of said liquor lance through at least three symmetrically arranged orifices or through a circular gap.
7. A process according to any one of claims 1 to 5, wherein the oxygen containing gas is passed through a diverging nozzle arranged coaxially around the liquor lance, which nozzle ends in the reaction zone of said reactor.
8. A process according to any one of claims 1 to 5, wherein the vortex blading is arranged substantially behind the atomizing nozzle of the liquor lance.
9. A process according to any one of claims 1 to 5, wherein the oxygen containing gas is preheated to above 100°C.
10. A process according to any one of claims 1 to 5, wherein the oxygen containing gas is preheated to above 300°C.
11. A process according to any one of claims 1 to 5, wherein the oxygen containing gas consists of air or oxygen enriched air.
12. A process according to any one of claims 1 to 5, wherein the viscosity of the cellulose spent liquor prior to atomization has been decreased to less than 200 cSt.
13. A process according to any one of claims 1 to 5, wherein the viscosity of the cellulose spent liquor prior to atomization has been decreased to less than 100 cSt.
14. A process according to any one of claims 1 to 5, wherein the cellulose spent liquor discharged into the reactor has a temperature above its boiling point at the prevailing reactor pressure.
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| SE9001958A SE466268B (en) | 1990-05-31 | 1990-05-31 | PROCEDURES FOR PARTIAL COMBUSTION OF BLACK FLOAT |
| SE9001958-9 | 1990-05-31 |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CA2043605A1 CA2043605A1 (en) | 1991-12-01 |
| CA2043605C true CA2043605C (en) | 2001-12-04 |
Family
ID=20379646
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CA002043605A Expired - Lifetime CA2043605C (en) | 1990-05-31 | 1991-05-30 | Process for the partial combustion of cellulose spent liquors |
Country Status (17)
| Country | Link |
|---|---|
| EP (1) | EP0459963B1 (en) |
| JP (1) | JP3050950B2 (en) |
| KR (1) | KR910020369A (en) |
| CN (1) | CN1035959C (en) |
| AT (1) | ATE127180T1 (en) |
| AU (1) | AU643522B2 (en) |
| BR (1) | BR9102205A (en) |
| CA (1) | CA2043605C (en) |
| DE (1) | DE69112496T2 (en) |
| ES (1) | ES2078500T3 (en) |
| FI (1) | FI101724B (en) |
| NO (1) | NO176365C (en) |
| NZ (1) | NZ238221A (en) |
| PT (1) | PT97792B (en) |
| RU (1) | RU2032126C1 (en) |
| SE (1) | SE466268B (en) |
| ZA (1) | ZA913732B (en) |
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| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| SE501334C2 (en) * | 1991-11-04 | 1995-01-16 | Kvaerner Pulping Tech | Methods of thermally decomposing a carbonaceous feedstock during sub-stoichiometric oxygen supply and apparatus for carrying out the method |
| SE470515B (en) * | 1992-11-02 | 1994-06-27 | Chemrec Ab | Process for producing hydrogen peroxide |
| US5628872A (en) * | 1993-10-22 | 1997-05-13 | Kanyr Ab | Method for bleaching pulp with hydrogen peroxide recovered from cellulosic spent liquor |
| FI107058B (en) * | 1996-10-07 | 2001-05-31 | Kvaerner Pulping Oy | Method for burning of waste liquor containing silicate |
| GB2450250B (en) | 2006-05-26 | 2009-08-12 | Alexsandra Byrne | Eyelash adornment |
| FI126455B (en) * | 2015-04-14 | 2016-12-15 | Fortum Oyj | Soda boiler, fuel feed means and process for feeding black liquor and air to reduce nitric oxide emissions |
Family Cites Families (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| SE137938C1 (en) * | ||||
| US3163495A (en) * | 1962-05-02 | 1964-12-29 | Greenawalt John Eckert | In the recovery of chemicals from the incineration of waste black liquor, the method f eliminating noxious compounds entrained in the combustion gas |
| SE453102B (en) * | 1985-01-22 | 1988-01-11 | Stiftelsen Cellulosa Och Pappe | KEEP ON BURNING OF MASS PREPARATION ACCORDING TO COOKING PROCESSES ON SODIUM BASE ERHALLEN INDUNSTAD END |
-
1990
- 1990-05-31 SE SE9001958A patent/SE466268B/en not_active Application Discontinuation
-
1991
- 1991-05-16 ZA ZA913732A patent/ZA913732B/en unknown
- 1991-05-16 ES ES91850130T patent/ES2078500T3/en not_active Expired - Lifetime
- 1991-05-16 DE DE69112496T patent/DE69112496T2/en not_active Expired - Fee Related
- 1991-05-16 AT AT91850130T patent/ATE127180T1/en active
- 1991-05-16 EP EP91850130A patent/EP0459963B1/en not_active Expired - Lifetime
- 1991-05-17 KR KR1019910008054A patent/KR910020369A/en not_active Application Discontinuation
- 1991-05-22 NZ NZ238221A patent/NZ238221A/en unknown
- 1991-05-22 AU AU77184/91A patent/AU643522B2/en not_active Ceased
- 1991-05-22 NO NO911969A patent/NO176365C/en unknown
- 1991-05-29 BR BR919102205A patent/BR9102205A/en not_active Application Discontinuation
- 1991-05-29 PT PT97792A patent/PT97792B/en not_active IP Right Cessation
- 1991-05-30 CA CA002043605A patent/CA2043605C/en not_active Expired - Lifetime
- 1991-05-30 FI FI912607A patent/FI101724B/en active
- 1991-05-30 RU SU914895672A patent/RU2032126C1/en active
- 1991-05-31 JP JP3155178A patent/JP3050950B2/en not_active Expired - Lifetime
- 1991-05-31 CN CN91103739A patent/CN1035959C/en not_active Expired - Fee Related
Also Published As
| Publication number | Publication date |
|---|---|
| FI912607A0 (en) | 1991-05-30 |
| FI101724B1 (en) | 1998-08-14 |
| DE69112496D1 (en) | 1995-10-05 |
| AU643522B2 (en) | 1993-11-18 |
| ES2078500T3 (en) | 1995-12-16 |
| AU7718491A (en) | 1991-12-05 |
| CA2043605A1 (en) | 1991-12-01 |
| PT97792A (en) | 1992-02-28 |
| ATE127180T1 (en) | 1995-09-15 |
| FI912607A (en) | 1991-12-01 |
| DE69112496T2 (en) | 1996-02-08 |
| PT97792B (en) | 1998-10-30 |
| ZA913732B (en) | 1992-02-26 |
| NO176365C (en) | 1995-03-22 |
| JP3050950B2 (en) | 2000-06-12 |
| NO176365B (en) | 1994-12-12 |
| SE466268B (en) | 1992-01-20 |
| NZ238221A (en) | 1993-10-26 |
| SE9001958L (en) | 1991-12-01 |
| CN1057500A (en) | 1992-01-01 |
| KR910020369A (en) | 1991-12-20 |
| EP0459963A1 (en) | 1991-12-04 |
| FI101724B (en) | 1998-08-14 |
| CN1035959C (en) | 1997-09-24 |
| NO911969D0 (en) | 1991-05-22 |
| SE9001958D0 (en) | 1990-05-31 |
| NO911969L (en) | 1991-12-02 |
| EP0459963B1 (en) | 1995-08-30 |
| JPH05140887A (en) | 1993-06-08 |
| RU2032126C1 (en) | 1995-03-27 |
| BR9102205A (en) | 1992-01-07 |
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