Technical field
[0001] The present invention relates to a process for partial combustion of cellulose spent
liquors from the cellulose industry in a burner connected to a reactor, which burner
comprises a centrally arranged burner gun or liquor lance equipped with a nozzle at
its front end which adds liquor and, a coaxially arranged tubular channel around the
liquor lance, in which channel an oxygen containing gas is added to support partial
combustion, whereby the oxygen containing gas, prior to entry in the coaxially arranged
channel, has been given a vortex movement.
[0002] 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
[0003] 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 recovered in a recovery boiler in which the black liquor is completely
burned.
[0004] Partial combustion of black liquor in a gasification reactor as in the present invention
generates a combustible gas comprising H₂, CO, CO₂, and droplets of molten inorganic
chemicals.
[0005] 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 spent
liquors generated in the cellulose industry can, after concentration, be used as a
feedstock in the process of the present invention.
[0006] Although the following description describes the present invention as it applies
to black liquor it is not restricted only to this particular liquor in its application.
[0007] 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.
[0008] 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.
[0009] As the exemplification below show, black liquor as a fuel is characterized by a relatively
low calorific value and high water and ash contents.

[0010] 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. The vortex burner described
in the present invention provides high combustion efficiency and flame stability using
black liquor as fuel in a relatively small reactor volume. The temperature 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 dioxide, 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.
[0011] The flow pattern near the burner is influenced to a great extent by the level of
vortex which can be controlled by e.g. adjusting the vortex blading. 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 recirculate 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.
[0012] The mixing of the liquor spray and the combustion air is supported by the turbulent
shear surface between the recirculation zone and the discharged gas and liquor droplets.
[0013] An outer recirculation zone, however, of less importance for the stability of the
flame is also developed. Its shape is influenced more by the geometry of the reactor
than by the geometry of the burner.
[0014] The degree of atomization of the liquor is of great importance for obtaining a stable
black liquor flame, the extension of the flame and high carbon conversion. The rheological
properties of the black liquor are of significant importance to the 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.
[0015] 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.
[0016] 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.
[0017] "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 the 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 invention
[0018] 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 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.
[0019] 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.
[0020] 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 recirculation,
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
zerovelocity 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 toroidal vortex is developed, an important advantage for the stability of the flame
and the course of the partial combustion.
[0021] 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 on the liquor lance 1 for
the purpose of adding black liquor and the later in contact with an inner concentric
annular tube 7 for the purpose of adding atomizing 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 tubes 6 and 7, and the concentric annular
tube 7. The black liquor is introduced into the liquor lance 1 through an inlet tube
20 and the air through another inlet tube 21.
[0022] 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 11, 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.
[0023] 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.
[0024] When designing burners great attention has to be paid to the weight relationship
between the air and fuel added.
[0025] The black liquor described herein is a fuel possessing unusual properties and thus
a burner which shall provide a stable flame must be designed accordingly.
[0026] 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.
[0027] 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.
[0028] The air/fuel ratio (by weight) for some fuels at stoichiometric combustion are exemplified
below:

[0029] 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 velocities the air should be preheated to at least 100°C, preferably
to 300°C 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 combustion can be added to the flame zone through the atomizing nozzle and
optionally, another part can be added through secondary air gates in the upper part
of the reactor.
1. Process for partial combustion of cellulose spent liquors using a burner connected
to a reactor while adding an oxygen containing gas, characterized in that a temperature of more than 700°C is maintained 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.
2. Process according to claim 1, characterized in that the weight ratio between oxygen added in the oxygen containing gas and the
cellulose spent liquor solids is 0.15-0.5:1.
3. Process according to claim 1, characterized in that the oxygen containing gas added through the coaxial channel has a vortex
movement.
4. Process according to claim 1, characterized in that the oxygen containing gas added through the coaxial channel is forced to
pass through vortex blading.
5. Process according to claim 1, characterized in that 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. Process according to one or more of claims 1 to 5, characterized in that 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. Process according to one or more of claims 1 to 6, characterized in that 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. Process according to one or more of claims 1 to 7, characterized in that the vortex blading is arranged substantially behind the atomizing nozzle
of the liquor lance.
9. Process according to one or more of claims 1 to 8, characterized in that the oxygen containing gas is preheated to above 100°C, preferably to above
300°C.
10. Process according to one or more of claims 1 to 9, characterized in that the oxygen containing gas consists of air or oxygen enriched air.
11. Process according to one or more of claims 1 to 10, characterized in that the viscosity of the cellulose spent liquor prior to atomization has been
decreased to less than 200 cSt, preferably to less than 100 cSt.
12. Process according to one or more of claims 1 to 11, characterized in that the cellulose spent liquor discharged into the reactor has a temperature
above its boiling point at the prevailing reactor pressure.