US2008839A - Method and means for cleaning sulphite cellulose preheaters - Google Patents
Method and means for cleaning sulphite cellulose preheaters Download PDFInfo
- Publication number
- US2008839A US2008839A US689048A US68904833A US2008839A US 2008839 A US2008839 A US 2008839A US 689048 A US689048 A US 689048A US 68904833 A US68904833 A US 68904833A US 2008839 A US2008839 A US 2008839A
- Authority
- US
- United States
- Prior art keywords
- liquid
- preheater
- incrustations
- circulating
- preheaters
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Lifetime
Links
- 238000000034 method Methods 0.000 title description 13
- 229920002678 cellulose Polymers 0.000 title description 12
- 239000001913 cellulose Substances 0.000 title description 12
- LSNNMFCWUKXFEE-UHFFFAOYSA-L sulfite Chemical compound [O-]S([O-])=O LSNNMFCWUKXFEE-UHFFFAOYSA-L 0.000 title description 12
- 238000004140 cleaning Methods 0.000 title description 9
- 239000007788 liquid Substances 0.000 description 36
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 14
- 239000012295 chemical reaction liquid Substances 0.000 description 8
- 238000009835 boiling Methods 0.000 description 4
- 229910052602 gypsum Inorganic materials 0.000 description 4
- 239000010440 gypsum Substances 0.000 description 4
- LSNNMFCWUKXFEE-UHFFFAOYSA-N Sulfurous acid Chemical compound OS(O)=O LSNNMFCWUKXFEE-UHFFFAOYSA-N 0.000 description 3
- 239000007789 gas Substances 0.000 description 3
- NLXLAEXVIDQMFP-UHFFFAOYSA-N Ammonia chloride Chemical compound [NH4+].[Cl-] NLXLAEXVIDQMFP-UHFFFAOYSA-N 0.000 description 2
- 235000008733 Citrus aurantifolia Nutrition 0.000 description 2
- FAPWRFPIFSIZLT-UHFFFAOYSA-M Sodium chloride Chemical compound [Na+].[Cl-] FAPWRFPIFSIZLT-UHFFFAOYSA-M 0.000 description 2
- 235000011941 Tilia x europaea Nutrition 0.000 description 2
- 230000015572 biosynthetic process Effects 0.000 description 2
- 238000007664 blowing Methods 0.000 description 2
- 230000007423 decrease Effects 0.000 description 2
- 238000010438 heat treatment Methods 0.000 description 2
- 239000004571 lime Substances 0.000 description 2
- 238000009825 accumulation Methods 0.000 description 1
- 235000019270 ammonium chloride Nutrition 0.000 description 1
- LVGQIQHJMRUCRM-UHFFFAOYSA-L calcium bisulfite Chemical compound [Ca+2].OS([O-])=O.OS([O-])=O LVGQIQHJMRUCRM-UHFFFAOYSA-L 0.000 description 1
- 235000010260 calcium hydrogen sulphite Nutrition 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 238000004090 dissolution Methods 0.000 description 1
- 239000012153 distilled water Substances 0.000 description 1
- 239000013505 freshwater Substances 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000001105 regulatory effect Effects 0.000 description 1
- 239000012266 salt solution Substances 0.000 description 1
- 239000011780 sodium chloride Substances 0.000 description 1
- 239000000243 solution Substances 0.000 description 1
- 238000002834 transmittance Methods 0.000 description 1
Images
Classifications
-
- 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
- D21C3/00—Pulping cellulose-containing materials
- D21C3/22—Other features of pulping processes
- D21C3/226—Use of compounds avoiding scale formation
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
- Y10S—TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10S159/00—Concentrating evaporators
- Y10S159/13—Scale
Definitions
- the present invention relates to improvements in methods and means to be used in connection with sulphite cellulose boilers of the kind, wherein an outer circulating system provided with pump is used for circulating the reaction liquid through an indirectly heated preheater.
- incrustations are deposited from time to time, particularly on the tube walls in the preheater.
- the danger of formation of such incrustations is different in different plants and may also vary during difierent seasons.
- the formation of incrustations is particularly extensive during the hot seasons.
- the incrustations consist, as tests have proved, almost entirely of gypsum and cause a considerable decrease of the heat transmittance in the preheater. It is therefore of great importance that they be removed from time to time. According to the invention this is carried out by circulating in a closed circulating system a liquid dissolving the incrustations, for example water.
- the circulating system consists at least of a pump and the preheater and the necessary conduits, and said circulation is to be carried out when the boiling 25 operation has been concluded, or the preheater has been shut off from the boiler. Finally the circulation is to be carried out with such a velocity of the liquid through the preheater that the flow of the liquid through the preheater becomes turbulent.
- Certain salt solutions have also the ability of dissolving more gypsum than pure water, such as solutions of ammonium chloride or sodium chloride.
- Fig. 1 is a partly sectional, diagrammatic view illustrating an apparatus suitable for carrying out the improved method
- FIG. 2 is a diagrammatic view of a modified form of apparatus.
- the simplest way of dissolving the incrustations in the preheater consists according to the invention in filling the boiler connected to the pre- 5 heater with water and thereupon starting circulation through a circulating system of the kind illustrated in Fig. 1.
- l designates the boiler, 2 and 2' the circulation conduits, 3 the circulation pump.
- 4 is the preheater provided 10 with steam supply conduit 5 and discharge conduit 6 for the water condensate.
- l is the gas discharge conduit from the boiler.
- the circulating system used for carrying out the method according to the invention is thus identical with the circulating system used in the ordinary boiling with the reaction liquid.
- the circulation may be carried out in such a way that a considerable part of the circulating liquid is led from the preheater to the pump by way of a by-pass conduit 9 past the container 8 so that only a minor part of liquid is passed through said container, as also illustrated in Fig. 1.
- Such a continuous or discontinuous introduction of new liquid and discharge oi used liquid may 01 course also be used in connection with circulating systems containing a separate tainer or the boiler, but is 01' course of less importance in such cases.
- Fig. 2 a modification of the arrangement just described is also illustrated. Instead of using the pump connected to the circulating system of the boilers, a separate pump it is used for circulating the liquid dissolving the incrustations. This pump as well as the container l in Fig. 1 may be common to a plurality of boilers.
- the method removing incrustations from indirectly heated preheaters for the reaction liquid in circulating systems for sulphite cellulose boilers, which comprises circulating a liquid capable of dissolving said incrustations through a closed circulating system containing said preheater, introducing i'resh liquid into the system during the circulation of said liquid and withdrawing a corresponding quantity of the used cleaning liquid.
- the method of removing incrustations from indirectly heated preheaters for the reaction liquid in circulating systems for sulphite cellulose boilers which comprises circulating a liquid capable of dissolving said'incrustations through a closed circulating system containing said preheater, simultaneously continually introducing *i'resh liquid into the system and continually withdrawing a corresponding quantity of the used cleaning liquid.
- the method of removing incrustations from indirectly heated preheaters tor the reaction-liquid in circulating systems for sulphite cellulose boilers which comprises circulating a liquid capable of dissolving said incrustations through a closed circulating system containing said preheater with such a velocity that the flow of said dissolving liquid through the preheater will be of a turbulent character, simultaneously continually introducing fresh liquid into the system and continually withdrawing a corresponding quantity of the used cleaning liquid.
- the method of removing incrustations from indirectly heated preheaters for the reaction liquid in circulating systems for sulphite cellulose boilers which comprises shutting oil the preheater from the boiler, circulating water containing an agent which facilitates the dissolution of said incrustations through a system containing said preheater with such a velocity that the flow through the tubes of the preheater is turbulent, simultaneously continually introducing fresh liquid into the system and withdrawing a corresponding quantity of used cleaning liquid.
- the method of removing incrustations from indirectly heated preheaters for the reaction liquid in circulating systems for sulphite cellulose boilers which comprises shutting oil the preheater from the boiler, circulating water containing sulphurous acid through a system containing said preheater with such a velocity that the flow through the tubes of the preheater is turbulent, simultaneously continually introducing fresh liquid into the system and withdrawing a corresponding quantity of used cleaning liquid.
- Means for removing incrustations from indirectly heated preheaters for the reaction liquid in circulating systems for sulphite cellulose boilers comprising conduits containing a pump and connected with the preheater to form a closed circulating system which system is provided with connecting conduits for introduction of fresh liquid into said system and for removal of used liquid out of the system.
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- Treating Waste Gases (AREA)
Description
J y 1935- T. SAMSON 2,008,839 mmnon AND mums FOR CLEANING SULPHITE CELLULOSE PREHEATER Filed Sept. 11. 1955 lJE NVEIYT k 7019.97? Sams n Patented July' 23, 1935 UNITED STATES METHOD AND MEANS FOR CLEANING SULPHITE CELLULOSE PREHEATERS Torsten Samson, Stockholm, Sweden Application September 11, 1933, Serial No. 689,048 In Sweden September 15, 1932 7 Claims.
The present invention relates to improvements in methods and means to be used in connection with sulphite cellulose boilers of the kind, wherein an outer circulating system provided with pump is used for circulating the reaction liquid through an indirectly heated preheater. In such preheaters incrustations are deposited from time to time, particularly on the tube walls in the preheater. The danger of formation of such incrustations is different in different plants and may also vary during difierent seasons. Thus the formation of incrustations is particularly extensive during the hot seasons.
The incrustations consist, as tests have proved, almost entirely of gypsum and cause a considerable decrease of the heat transmittance in the preheater. It is therefore of great importance that they be removed from time to time. According to the invention this is carried out by circulating in a closed circulating system a liquid dissolving the incrustations, for example water. The circulating system consists at least of a pump and the preheater and the necessary conduits, and said circulation is to be carried out when the boiling 25 operation has been concluded, or the preheater has been shut off from the boiler. Finally the circulation is to be carried out with such a velocity of the liquid through the preheater that the flow of the liquid through the preheater becomes turbulent.
ticularly suitable. However, as such a liquid only seldom is available, common water must usually be used. This contains, however, lime which decreases the ability of the water of dissolving the incrustations. To the water may therefore in a way known per se be added sulphurous acid which together with the lime in the water forms calcium bisulphite that does not act injuriously upon the solubility of the incrustations (the gypsum). In a sulphite cellulose plant sulphurous acid is always available, for example in the gases obtained at the blowing of the boilers, which gases may be utilized for said purpose.
Certain salt solutions have also the ability of dissolving more gypsum than pure water, such as solutions of ammonium chloride or sodium chloride.
The method according to the invention is to be carried out as described below with reference to the accompanyin drawing, in which,
Fig. 1 is a partly sectional, diagrammatic view illustrating an apparatus suitable for carrying out the improved method; and
As incrustation dissolver distilled water is par- Fig. 2 is a diagrammatic view of a modified form of apparatus.
The simplest way of dissolving the incrustations in the preheater consists according to the invention in filling the boiler connected to the pre- 5 heater with water and thereupon starting circulation through a circulating system of the kind illustrated in Fig. 1. In this figure, l designates the boiler, 2 and 2' the circulation conduits, 3 the circulation pump. 4 is the preheater provided 10 with steam supply conduit 5 and discharge conduit 6 for the water condensate. l is the gas discharge conduit from the boiler. When the preheater is to be cleansed from incrustations, the water is led from the boiler I through the conduit 2 to the pump 3 and from there through the preheater 4 and the conduits 2 back to the boiler.
In this case the circulating system used for carrying out the method according to the invention is thus identical with the circulating system used in the ordinary boiling with the reaction liquid.
It is then, however, necessary that the boiler be put out of operation during the period necessary for cleansing the preheater. To avoid this one may, as shown in Fig. 1, use a separate container 8 arranged outside of the boiler, and circulate the water or other liquid dissolving the incrustations through the conduit l2, the pump 3, the preheater 4, the conduit I3 and said container 8.
If found suitable, the circulation may be carried out in such a way that a considerable part of the circulating liquid is led from the preheater to the pump by way of a by-pass conduit 9 past the container 8 so that only a minor part of liquid is passed through said container, as also illustrated in Fig. 1.
However, it is not necessary to circulate the liquid through a container. In such a case new dissolving liquid should be introduced continuously or discontinuously into the circulating system and already used liquid be removed in a corresponding way. Such an arrangement is illustrated in Fig. 2, wherein the boiler I as usual is connected to the pump 3 and the preheater 4 by way of the usual circulation conduits 2 and 2' provided for the boiler. For cleansing the preheater 4 from incrustations one may use the circulating system 3, 4, 9, 2. New dissolving liquid is admitted through the conduit II and already used liquid is discharged through the conduit ID. The quantity of liquid is suitably so regulated that the concentration of dissolved gypsum (incrustations) in the discharged liquid will not be too high.
Such a continuous or discontinuous introduction of new liquid and discharge oi used liquid may 01 course also be used in connection with circulating systems containing a separate tainer or the boiler, but is 01' course of less importance in such cases.
In Fig. 2 a modification of the arrangement just described is also illustrated. Instead of using the pump connected to the circulating system of the boilers, a separate pump it is used for circulating the liquid dissolving the incrustations. This pump as well as the container l in Fig. 1 may be common to a plurality of boilers.
Tests made have proved that by circulating a liquid dissolving the incrustations through a" closed circulating system with the above mentloned velocity between the boiling processes, that is during the periods of blowing, emptying and charging the boilers, the heating surfaces of the preheater can be kept clean from incrustations, even under difllcult working conditions. This makes available the use of higher temperatures and consequently higher pressures, which have heretofore been objectionable because of the enormous accumulation of incrustation that was engendered by such higher temperatures. On account thereoi the heating operation may also be accelerated and the boiling period shortened, which means that an improved economy in the manufacture of the cellulose will be attained. Thus the invention involves an important technical progress.
Having now particularly described the nature of my invention and the manner 01 its operation, what I claim is:
1. The method removing incrustations from indirectly heated preheaters for the reaction liquid in circulating systems for sulphite cellulose boilers, which comprises circulating a liquid capable of dissolving said incrustations through a closed circulating system containing said preheater, introducing i'resh liquid into the system during the circulation of said liquid and withdrawing a corresponding quantity of the used cleaning liquid.
2. The method of removing incrustations from indirectly heated preheaters for the reaction liquid in circulating systems for sulphite cellulose boilers, which comprises circulating a liquid capable of dissolving said'incrustations through a closed circulating system containing said preheater, simultaneously continually introducing *i'resh liquid into the system and continually withdrawing a corresponding quantity of the used cleaning liquid.
3. The method of removing incrustations from indirectly heated preheaters tor the reaction-liquid in circulating systems for sulphite cellulose boilers, which comprises circulating a liquid capable of dissolving said incrustations through a closed circulating system containing said preheater with such a velocity that the flow of said dissolving liquid through the preheater will be of a turbulent character, simultaneously continually introducing fresh liquid into the system and continually withdrawing a corresponding quantity of the used cleaning liquid.
4. The method of removing incrustations from indirectly heated preheaters tor the reaction .iiquid in. circulating systems for sulphite celluose boilers, which comprises shutting oil the preheater from the boiler, circulating water through a closed circulating system containing said preheater with such a velocity that the flow through the tubes or the preheater is turbulent,-simultaneously continually introducing fresh water into the system and withdrawing a corresponding quantity of used cleaning liquid.
5. The method of removing incrustations from indirectly heated preheaters for the reaction liquid in circulating systems for sulphite cellulose boilers, which comprises shutting oil the preheater from the boiler, circulating water containing an agent which facilitates the dissolution of said incrustations through a system containing said preheater with such a velocity that the flow through the tubes of the preheater is turbulent, simultaneously continually introducing fresh liquid into the system and withdrawing a corresponding quantity of used cleaning liquid.
6. The method of removing incrustations from indirectly heated preheaters for the reaction liquid in circulating systems for sulphite cellulose boilers, which comprises shutting oil the preheater from the boiler, circulating water containing sulphurous acid through a system containing said preheater with such a velocity that the flow through the tubes of the preheater is turbulent, simultaneously continually introducing fresh liquid into the system and withdrawing a corresponding quantity of used cleaning liquid.
7. Means for removing incrustations from indirectly heated preheaters for the reaction liquid in circulating systems for sulphite cellulose boilers, comprising conduits containing a pump and connected with the preheater to form a closed circulating system which system is provided with connecting conduits for introduction of fresh liquid into said system and for removal of used liquid out of the system.
TORSTEN SAMSON.
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| SE2008839X | 1932-09-15 |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US2008839A true US2008839A (en) | 1935-07-23 |
Family
ID=20424309
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US689048A Expired - Lifetime US2008839A (en) | 1932-09-15 | 1933-09-11 | Method and means for cleaning sulphite cellulose preheaters |
Country Status (1)
| Country | Link |
|---|---|
| US (1) | US2008839A (en) |
Cited By (12)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2516076A (en) * | 1944-12-09 | 1950-07-18 | Pacific Flush Tank Co | Method of digesting sewage sludge or trades wastes |
| US2524757A (en) * | 1945-05-17 | 1950-10-10 | Dow Chemical Co | Cleaning scaled vessels |
| US2572767A (en) * | 1948-11-18 | 1951-10-23 | Pacific Flush Tank Co | Method and apparatus for digesting garbage and sewage sludge |
| US3170815A (en) * | 1961-08-10 | 1965-02-23 | Dow Chemical Co | Removal of calcium sulfate deposits |
| US3240627A (en) * | 1961-08-10 | 1966-03-15 | Dow Chemical Co | Removal of calcium sulfate deposits |
| US3272652A (en) * | 1961-01-06 | 1966-09-13 | Whirlpool Co | Method of removing film deposits |
| US3298931A (en) * | 1962-01-15 | 1967-01-17 | Commw Scient Ind Res Org | Removal of scale in distillation of sea water containing magnesium salts |
| US3441035A (en) * | 1965-11-19 | 1969-04-29 | Atomic Energy Authority Uk | Pickling apparatus |
| US3754967A (en) * | 1971-06-18 | 1973-08-28 | Dow Corning | Method of adhering silicone rubber to metal surfaces using salts |
| EP0313730A1 (en) * | 1987-10-26 | 1989-05-03 | Kamyr, Inc. | Apparatus and methods for reducing the formation of scale in pulping operations |
| WO2002046680A1 (en) * | 2000-12-07 | 2002-06-13 | Stora Kopparbergs Bergslags Ab | A method or removing deposits that are difficult to dissolve |
| WO2002083578A3 (en) * | 2001-04-16 | 2003-01-09 | Buckman Labor Inc | Process and apparatus for the removal of scale build-up |
-
1933
- 1933-09-11 US US689048A patent/US2008839A/en not_active Expired - Lifetime
Cited By (13)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2516076A (en) * | 1944-12-09 | 1950-07-18 | Pacific Flush Tank Co | Method of digesting sewage sludge or trades wastes |
| US2524757A (en) * | 1945-05-17 | 1950-10-10 | Dow Chemical Co | Cleaning scaled vessels |
| US2572767A (en) * | 1948-11-18 | 1951-10-23 | Pacific Flush Tank Co | Method and apparatus for digesting garbage and sewage sludge |
| US3272652A (en) * | 1961-01-06 | 1966-09-13 | Whirlpool Co | Method of removing film deposits |
| US3170815A (en) * | 1961-08-10 | 1965-02-23 | Dow Chemical Co | Removal of calcium sulfate deposits |
| US3240627A (en) * | 1961-08-10 | 1966-03-15 | Dow Chemical Co | Removal of calcium sulfate deposits |
| US3298931A (en) * | 1962-01-15 | 1967-01-17 | Commw Scient Ind Res Org | Removal of scale in distillation of sea water containing magnesium salts |
| US3441035A (en) * | 1965-11-19 | 1969-04-29 | Atomic Energy Authority Uk | Pickling apparatus |
| US3754967A (en) * | 1971-06-18 | 1973-08-28 | Dow Corning | Method of adhering silicone rubber to metal surfaces using salts |
| EP0313730A1 (en) * | 1987-10-26 | 1989-05-03 | Kamyr, Inc. | Apparatus and methods for reducing the formation of scale in pulping operations |
| WO2002046680A1 (en) * | 2000-12-07 | 2002-06-13 | Stora Kopparbergs Bergslags Ab | A method or removing deposits that are difficult to dissolve |
| WO2002083578A3 (en) * | 2001-04-16 | 2003-01-09 | Buckman Labor Inc | Process and apparatus for the removal of scale build-up |
| US6716307B2 (en) | 2001-04-16 | 2004-04-06 | Buckman Laboratories International, Inc. | Process and system for the removal of scale build-up |
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