US726036A - Process of utilizing sulfite lyes. - Google Patents
Process of utilizing sulfite lyes. Download PDFInfo
- Publication number
- US726036A US726036A US8364901A US1901083649A US726036A US 726036 A US726036 A US 726036A US 8364901 A US8364901 A US 8364901A US 1901083649 A US1901083649 A US 1901083649A US 726036 A US726036 A US 726036A
- Authority
- US
- United States
- Prior art keywords
- soda
- liquor
- spent
- mill
- pulp
- 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 15
- LSNNMFCWUKXFEE-UHFFFAOYSA-N Sulfurous acid Chemical compound OS(O)=O LSNNMFCWUKXFEE-UHFFFAOYSA-N 0.000 title description 8
- CDBYLPFSWZWCQE-UHFFFAOYSA-L Sodium Carbonate Chemical compound [Na+].[Na+].[O-]C([O-])=O CDBYLPFSWZWCQE-UHFFFAOYSA-L 0.000 description 13
- ODINCKMPIJJUCX-UHFFFAOYSA-N Calcium oxide Chemical compound [Ca]=O ODINCKMPIJJUCX-UHFFFAOYSA-N 0.000 description 6
- 239000002253 acid Substances 0.000 description 4
- 238000010411 cooking Methods 0.000 description 4
- DGAQECJNVWCQMB-PUAWFVPOSA-M Ilexoside XXIX Chemical compound C[C@@H]1CC[C@@]2(CC[C@@]3(C(=CC[C@H]4[C@]3(CC[C@@H]5[C@@]4(CC[C@@H](C5(C)C)OS(=O)(=O)[O-])C)C)[C@@H]2[C@]1(C)O)C)C(=O)O[C@H]6[C@@H]([C@H]([C@@H]([C@H](O6)CO)O)O)O.[Na+] DGAQECJNVWCQMB-PUAWFVPOSA-M 0.000 description 3
- 239000000292 calcium oxide Substances 0.000 description 3
- 235000012255 calcium oxide Nutrition 0.000 description 3
- 150000003839 salts Chemical class 0.000 description 3
- 229910052708 sodium Inorganic materials 0.000 description 3
- 239000011734 sodium Substances 0.000 description 3
- 235000017550 sodium carbonate Nutrition 0.000 description 3
- 229910000029 sodium carbonate Inorganic materials 0.000 description 3
- 239000002699 waste material Substances 0.000 description 3
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 2
- DWAQJAXMDSEUJJ-UHFFFAOYSA-M Sodium bisulfite Chemical compound [Na+].OS([O-])=O DWAQJAXMDSEUJJ-UHFFFAOYSA-M 0.000 description 2
- 150000007513 acids Chemical class 0.000 description 2
- 150000001299 aldehydes Chemical class 0.000 description 2
- 230000015572 biosynthetic process Effects 0.000 description 2
- 239000003518 caustics Substances 0.000 description 2
- 238000001704 evaporation Methods 0.000 description 2
- 238000010438 heat treatment Methods 0.000 description 2
- 238000002386 leaching Methods 0.000 description 2
- 230000003472 neutralizing effect Effects 0.000 description 2
- 229940001607 sodium bisulfite Drugs 0.000 description 2
- 235000010267 sodium hydrogen sulphite Nutrition 0.000 description 2
- 159000000000 sodium salts Chemical class 0.000 description 2
- GRVFOGOEDUUMBP-UHFFFAOYSA-N sodium sulfide (anhydrous) Chemical compound [Na+].[Na+].[S-2] GRVFOGOEDUUMBP-UHFFFAOYSA-N 0.000 description 2
- 150000003460 sulfonic acids Chemical class 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- CXRFDZFCGOPDTD-UHFFFAOYSA-M Cetrimide Chemical compound [Br-].CCCCCCCCCCCCCC[N+](C)(C)C CXRFDZFCGOPDTD-UHFFFAOYSA-M 0.000 description 1
- 150000001298 alcohols Chemical class 0.000 description 1
- 239000003513 alkali Substances 0.000 description 1
- 238000001354 calcination Methods 0.000 description 1
- 238000002485 combustion reaction Methods 0.000 description 1
- 238000009833 condensation Methods 0.000 description 1
- 230000005494 condensation Effects 0.000 description 1
- 230000008020 evaporation Effects 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- 229910052742 iron Inorganic materials 0.000 description 1
- 229910052979 sodium sulfide Inorganic materials 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01D—COMPOUNDS OF ALKALI METALS, i.e. LITHIUM, SODIUM, POTASSIUM, RUBIDIUM, CAESIUM, OR FRANCIUM
- C01D3/00—Halides of sodium, potassium or alkali metals in general
- C01D3/04—Chlorides
- C01D3/08—Preparation by working up natural or industrial salt mixtures or siliceous minerals
-
- 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
- Y10S423/00—Chemistry of inorganic compounds
- Y10S423/03—Papermaking liquor
Definitions
- This invention relates to certain iinprovetained in the sulfite lye and prevent thereby ments in the process of utilizing sulfite lyes, the formation from organic compoundsinthe I for which Letters Patent were granted to us lyes of the objectionable aldehydes. on March 7, 1899, No. 620,755, said improve- It is a well-known fact that in evaporating i5 ments being designed with a view of simplithe spent liquor from a soda-pulp mill there fying and cheapening the process and ad-aptis always a loss of atleast ten per cent.
- our invention consists of as the latter cannot be neutralized in the a process of neutralizing, the waste or spent steam-space of the boiler'they are carried on liquors of sulfite and soda pulp mills by first with the condensed water, and consequently neutralizing the waste liquor from one mill 4o corrode the iron and the multiple-concentratwith the sodium-containing liquor from the ing apparatus.
- WVe have found that this other mill; second, concentrating the neugeneration of acids can be considerably detralized liquors; third, burning concentrated creased when the temperature or the presliquors; fourth, leaching the residuum; fifth, ture in the boiler is kept down; but this im treating the solution with burnt lime, so as 45 pairs the efficiency and economy of the conto render it caustic, and then draining oflf the centrating efliect.
- iVe have further found clear liquor containing the soluble sodium that where the spent liquor from a soda-pulp salts for use as cooking liquor in the sodamill is obtainable the spent'liquor from a sulpulp mill.
- Our improved process has a special advantage in such cases where sulfite and soda pulp mills are run in one establishment or in close proximity, so that the spent liquors from both mills are available for use.
- the spent liquors from both mills can be utilized to great advantage by a comparatively simple process, the spent liquor from one mill being utilized for working up the spent liquor-of the other mill, the resulting liquor containing all the soluble sodium salts,
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Life Sciences & Earth Sciences (AREA)
- General Life Sciences & Earth Sciences (AREA)
- Geochemistry & Mineralogy (AREA)
- Geology (AREA)
- Engineering & Computer Science (AREA)
- Materials Engineering (AREA)
- Inorganic Chemistry (AREA)
- Paper (AREA)
Description
' UNITED" STAT S PATENT OFFICE.
VIGGO DREWSEN, OF NElV YORK, N. Y., AND LAURITZ J. DORENFELDT, OF
' TRONDHJEM, NORWAY.
PROCESS OF UTILI-ZING SULFITE LYES.
SPECIFICATION forming part Of Letters Patent N0. 726,036, dated April 21, 1903. Application filed November 25, 1901. seria No. 83,649. (No specimens.)
To all whom it may-concern: other words, the spent liquors from both Be it known that-we, VIGGO'DREWSEN, remillssulfite and soda pulp mills-can be sidingin New York,borough of Rich mond,and utilized to ad vantage in our improved process.
State of New York, and LAURITZ J. DOREN- While in our former process referred to re- 5 FELDT, residing in Trondhjem, in the King covered soda (soda-ash) was mixed with the dom of Norway, both citizens of the Kingdom sulfite lye, we now mix therewith the spent of Norway, have invented certain new and lye from the soda-pulp mill. The theory of useful Improvementsin Processes ofUtilizing the new process is that the sodium sulfide con- Sulfite Ly-es, of which the following is a specitained in the lye from the soda-mill react with Io fication. l .the salts of the organic sulfonic acids con- This invention relates to certain iinprovetained in the sulfite lye and prevent thereby ments in the process of utilizing sulfite lyes, the formation from organic compoundsinthe I for which Letters Patent were granted to us lyes of the objectionable aldehydes. on March 7, 1899, No. 620,755, said improve- It is a well-known fact that in evaporating i5 ments being designed with a view of simplithe spent liquor from a soda-pulp mill there fying and cheapening the process and ad-aptis always a loss of atleast ten per cent. of ing the same for use in sulfite-pulp mills, soda-ash, while when the spent liquor from which are run in connection with and in p'rox. a soda-pulp mill is worked up with the spent imity to soda-pulp mills. liquor from a sulfite-pulp mill, which latter 7o 20 We have found by practical tests in-sulfiteworks with sodium-bisulfite liquor, and both pulp mills that the process heretofore pat- 'liquors are evaporated together the sodium ented could be simplified when the waste liqcontained in the spent liquor from the sulfitenor from soda-pulp mills was employed for mill is sufficient to cover the loss of soda-ash Working up the spent liquor of the sulfite from the soda-pulp mill, so that there is no 25 pulp mills. We have also discovered that additional expense for soda for the sulfitewhen the spentliquor from sulfite-pulp mills pulp mill, inasmuch as the soda used in this was utilized by our patented process, even mill is recovered and utilized over again in with an excess of alkali, acid condensations the soda-pulp mill. Oonsequentlybycarrying are produced which corrode the concentrat on the evaporation of the spent liquors from 3o ing apparatus, for the reason that when the a soda-pulp mill mixed with those of asulfitetemperature, and consequently the pressure pulp mill a very economical process is obin'the boiler in which the spent liquoris contained by which the spent liquors of both centrated, rises to a high temperature vapors mills are utilized and at the same time the are given 01f which contain aldehydes that polution of the water-courses in the neigh- 35 are decomposed when mixed with steam of boI-hood of the mills eflectively prevented.-
high temperature into alcohols and acids, and Forthis purpose our invention consists of as the latter cannot be neutralized in the a process of neutralizing, the waste or spent steam-space of the boiler'they are carried on liquors of sulfite and soda pulp mills by first with the condensed water, and consequently neutralizing the waste liquor from one mill 4o corrode the iron and the multiple-concentratwith the sodium-containing liquor from the ing apparatus. WVe have found that this other mill; second, concentrating the neugeneration of acids can be considerably detralized liquors; third, burning concentrated creased when the temperature or the presliquors; fourth, leaching the residuum; fifth, ture in the boiler is kept down; but this im treating the solution with burnt lime, so as 45 pairs the efficiency and economy of the conto render it caustic, and then draining oflf the centrating efliect. iVe have further found clear liquor containing the soluble sodium that where the spent liquor from a soda-pulp salts for use as cooking liquor in the sodamill is obtainable the spent'liquor from a sulpulp mill. v fits-pulp mill can be utilized with this alka- Our process is practically carried out as I00 50 line liquor without any formation of acid follows: The spent cooking liquor from asultaking place in the concentrating plant. In fito-pulp mill which contains sodium bisulfite is neutralized by an equal quantity otthe' The hot gases which are developed by the combustion are carried off. and utilized for heating purposes, preferably for heating the boiler or the vacuum-pan itself, while the inorganic residuum is leached with water. The solution thus obtained is treated with burnt lime, so as to render it caustic, and is then drawn off and added to'the cooking liquor of the soda-pulpmill, the solution containing all the soluble sodium salts.
Our improved process has a special advantage in such cases where sulfite and soda pulp mills are run in one establishment or in close proximity, so that the spent liquors from both mills are available for use. In this case the spent liquors from both mills can be utilized to great advantage by a comparatively simple process, the spent liquor from one mill being utilized for working up the spent liquor-of the other mill, the resulting liquor containing all the soluble sodium salts,
which are then returned to the soda-pulp mill for being utilized as cooking liquor in the same. I
Having thus described our invention we claim as new and desire to secure by Le ters Patent- The process herein described of utilizing thewaste liquors of sulfite and soda pulp mill liquor containing salts of organic sulfonic acids with the liquor from the soda-pulp mill containing sodium sulfid, concentrating the neutralized liquor, calcining the concentrated liquor, leaching the residuum obtained thereby, treating the solution thus obtained with 'burnt lime, and draining off the soluble VIGGO DREWSEN. LAURITZ J. DORENFELDT.
Witnesses:
PAUL GOEPEL, HENRY SUHRBIER.
mills,which consists in neutralizing the sulfite- I
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US8364901A US726036A (en) | 1901-11-25 | 1901-11-25 | Process of utilizing sulfite lyes. |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US8364901A US726036A (en) | 1901-11-25 | 1901-11-25 | Process of utilizing sulfite lyes. |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US726036A true US726036A (en) | 1903-04-21 |
Family
ID=2794546
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US8364901A Expired - Lifetime US726036A (en) | 1901-11-25 | 1901-11-25 | Process of utilizing sulfite lyes. |
Country Status (1)
| Country | Link |
|---|---|
| US (1) | US726036A (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2747552A (en) * | 1952-04-05 | 1956-05-29 | Kyrklund Gunnar | Method of generating vapour from waste sulfite liquor or dregs |
| US2898994A (en) * | 1953-03-31 | 1959-08-11 | Alfred M Thomsen | Method of making paper pulp |
-
1901
- 1901-11-25 US US8364901A patent/US726036A/en not_active Expired - Lifetime
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2747552A (en) * | 1952-04-05 | 1956-05-29 | Kyrklund Gunnar | Method of generating vapour from waste sulfite liquor or dregs |
| US2898994A (en) * | 1953-03-31 | 1959-08-11 | Alfred M Thomsen | Method of making paper pulp |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| JPS5484892A (en) | Electrolysis of sodium chloride employing cation exchange membrane | |
| US3714911A (en) | Method of treatment of alkaline pulping black liquors by wet air oxidation | |
| US2238456A (en) | Purification of magnesium base liquors | |
| US2069185A (en) | Manufacture of vanillin from waste sulphite pulp liquor | |
| US726036A (en) | Process of utilizing sulfite lyes. | |
| US1149420A (en) | Process of utilizing the organic as well as the inorganic constituents of the waste liquor produced by the boiling of sulfite cellulose. | |
| US2656245A (en) | Preparation of sodium salts of carbonic acid by ion exchange | |
| US2824071A (en) | Recovery of chemicals in wood pulp preparation | |
| US1605927A (en) | Sodium-monosulphite waste-liquor-recovery process | |
| US2029616A (en) | Process for preparing alkali sulphite or alkali bisulphite solutions from waste liquors obtained in the digestion of cellulose with alkali sulphur compounds | |
| US1779535A (en) | Process of treating black liquors | |
| US2611682A (en) | Methods of recovering hydrogen sulfide from sulfide containing soda liquors obtainedin cellulose production | |
| US2913310A (en) | Chemical recovery process | |
| US3674630A (en) | Kraft liquor recovery system including physically isolated oxidation and reduction stages | |
| US1488829A (en) | Process of making cooking liquors | |
| US2774754A (en) | Method of disposing and utilization of sulfite waste liquor | |
| US3326980A (en) | Preparation of methyl mercaptan from waste pulping liquors | |
| US2047032A (en) | Process of correlating chemical recovery in pulp mills operating with different kinds of liquors | |
| US2204522A (en) | Operation of steam turbines | |
| US1402173A (en) | Process for obtaining potassium chloride | |
| US3740309A (en) | Process for treating ammonia-base waste sulfite liquor | |
| JPS5836291A (en) | Alkaline pulping chemical recovery system | |
| US1580269A (en) | Process for regenerating black liquor | |
| US3057770A (en) | Method for the recovery of spent sulphite liquors | |
| Spruill | Paper Mill Waste: Treatment for Color Removal |