US1056366A - Sulfite-waste explosive. - Google Patents
Sulfite-waste explosive. Download PDFInfo
- Publication number
- US1056366A US1056366A US69018412A US1912690184A US1056366A US 1056366 A US1056366 A US 1056366A US 69018412 A US69018412 A US 69018412A US 1912690184 A US1912690184 A US 1912690184A US 1056366 A US1056366 A US 1056366A
- Authority
- US
- United States
- Prior art keywords
- sulfite
- liquors
- waste
- explosive
- ingredients
- 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
- 239000002360 explosive Substances 0.000 title description 21
- 239000002699 waste material Substances 0.000 title description 20
- LSNNMFCWUKXFEE-UHFFFAOYSA-N Sulfurous acid Chemical compound OS(O)=O LSNNMFCWUKXFEE-UHFFFAOYSA-N 0.000 description 22
- 239000000470 constituent Substances 0.000 description 14
- 239000004615 ingredient Substances 0.000 description 12
- 238000000034 method Methods 0.000 description 11
- 239000000463 material Substances 0.000 description 9
- 239000007800 oxidant agent Substances 0.000 description 9
- PAWQVTBBRAZDMG-UHFFFAOYSA-N 2-(3-bromo-2-fluorophenyl)acetic acid Chemical compound OC(=O)CC1=CC=CC(Br)=C1F PAWQVTBBRAZDMG-UHFFFAOYSA-N 0.000 description 8
- 238000002156 mixing Methods 0.000 description 8
- 229920002522 Wood fibre Polymers 0.000 description 7
- 239000002025 wood fiber Substances 0.000 description 7
- 238000001704 evaporation Methods 0.000 description 6
- 239000002023 wood Substances 0.000 description 6
- 230000008020 evaporation Effects 0.000 description 5
- 239000007788 liquid Substances 0.000 description 4
- 239000002245 particle Substances 0.000 description 4
- 229910002651 NO3 Inorganic materials 0.000 description 3
- NHNBFGGVMKEFGY-UHFFFAOYSA-N Nitrate Chemical compound [O-][N+]([O-])=O NHNBFGGVMKEFGY-UHFFFAOYSA-N 0.000 description 3
- 239000003513 alkali Substances 0.000 description 3
- 229920002678 cellulose Polymers 0.000 description 3
- 239000001913 cellulose Substances 0.000 description 3
- 238000007580 dry-mixing Methods 0.000 description 3
- 239000000203 mixture Substances 0.000 description 3
- 230000001590 oxidative effect Effects 0.000 description 3
- 239000000126 substance Substances 0.000 description 3
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 2
- OYPRJOBELJOOCE-UHFFFAOYSA-N Calcium Chemical compound [Ca] OYPRJOBELJOOCE-UHFFFAOYSA-N 0.000 description 2
- 235000008733 Citrus aurantifolia Nutrition 0.000 description 2
- SRBFZHDQGSBBOR-IOVATXLUSA-N D-xylopyranose Chemical compound O[C@@H]1COC(O)[C@H](O)[C@H]1O SRBFZHDQGSBBOR-IOVATXLUSA-N 0.000 description 2
- 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 2
- 235000011941 Tilia x europaea Nutrition 0.000 description 2
- 239000002253 acid Substances 0.000 description 2
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 2
- 239000011575 calcium Substances 0.000 description 2
- 229910052791 calcium Inorganic materials 0.000 description 2
- OSGAYBCDTDRGGQ-UHFFFAOYSA-L calcium sulfate Chemical compound [Ca+2].[O-]S([O-])(=O)=O OSGAYBCDTDRGGQ-UHFFFAOYSA-L 0.000 description 2
- 150000001875 compounds Chemical class 0.000 description 2
- 229920005610 lignin Polymers 0.000 description 2
- 239000004571 lime Substances 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 229910052760 oxygen Inorganic materials 0.000 description 2
- 239000001301 oxygen Substances 0.000 description 2
- FGIUAXJPYTZDNR-UHFFFAOYSA-N potassium nitrate Chemical compound [K+].[O-][N+]([O-])=O FGIUAXJPYTZDNR-UHFFFAOYSA-N 0.000 description 2
- 235000011152 sodium sulphate Nutrition 0.000 description 2
- 238000003756 stirring Methods 0.000 description 2
- TUSDEZXZIZRFGC-UHFFFAOYSA-N 1-O-galloyl-3,6-(R)-HHDP-beta-D-glucose Natural products OC1C(O2)COC(=O)C3=CC(O)=C(O)C(O)=C3C3=C(O)C(O)=C(O)C=C3C(=O)OC1C(O)C2OC(=O)C1=CC(O)=C(O)C(O)=C1 TUSDEZXZIZRFGC-UHFFFAOYSA-N 0.000 description 1
- SPSSULHKWOKEEL-UHFFFAOYSA-N 2,4,6-trinitrotoluene Chemical compound CC1=C([N+]([O-])=O)C=C([N+]([O-])=O)C=C1[N+]([O-])=O SPSSULHKWOKEEL-UHFFFAOYSA-N 0.000 description 1
- QGZKDVFQNNGYKY-UHFFFAOYSA-O Ammonium Chemical compound [NH4+] QGZKDVFQNNGYKY-UHFFFAOYSA-O 0.000 description 1
- 241000406799 Deto Species 0.000 description 1
- 239000001263 FEMA 3042 Substances 0.000 description 1
- WQZGKKKJIJFFOK-GASJEMHNSA-N Glucose Natural products OC[C@H]1OC(O)[C@H](O)[C@@H](O)[C@@H]1O WQZGKKKJIJFFOK-GASJEMHNSA-N 0.000 description 1
- 229920001732 Lignosulfonate Polymers 0.000 description 1
- FYYHWMGAXLPEAU-UHFFFAOYSA-N Magnesium Chemical compound [Mg] FYYHWMGAXLPEAU-UHFFFAOYSA-N 0.000 description 1
- SNIOPGDIGTZGOP-UHFFFAOYSA-N Nitroglycerin Chemical compound [O-][N+](=O)OCC(O[N+]([O-])=O)CO[N+]([O-])=O SNIOPGDIGTZGOP-UHFFFAOYSA-N 0.000 description 1
- 239000000006 Nitroglycerin Substances 0.000 description 1
- LRBQNJMCXXYXIU-PPKXGCFTSA-N Penta-digallate-beta-D-glucose Natural products OC1=C(O)C(O)=CC(C(=O)OC=2C(=C(O)C=C(C=2)C(=O)OC[C@@H]2[C@H]([C@H](OC(=O)C=3C=C(OC(=O)C=4C=C(O)C(O)=C(O)C=4)C(O)=C(O)C=3)[C@@H](OC(=O)C=3C=C(OC(=O)C=4C=C(O)C(O)=C(O)C=4)C(O)=C(O)C=3)[C@H](OC(=O)C=3C=C(OC(=O)C=4C=C(O)C(O)=C(O)C=4)C(O)=C(O)C=3)O2)OC(=O)C=2C=C(OC(=O)C=3C=C(O)C(O)=C(O)C=3)C(O)=C(O)C=2)O)=C1 LRBQNJMCXXYXIU-PPKXGCFTSA-N 0.000 description 1
- 229920001131 Pulp (paper) Polymers 0.000 description 1
- -1 aceticaci'd Chemical compound 0.000 description 1
- 229910021529 ammonia Inorganic materials 0.000 description 1
- DVARTQFDIMZBAA-UHFFFAOYSA-O ammonium nitrate Chemical compound [NH4+].[O-][N+]([O-])=O DVARTQFDIMZBAA-UHFFFAOYSA-O 0.000 description 1
- BFNBIHQBYMNNAN-UHFFFAOYSA-N ammonium sulfate Chemical compound N.N.OS(O)(=O)=O BFNBIHQBYMNNAN-UHFFFAOYSA-N 0.000 description 1
- 229910052921 ammonium sulfate Inorganic materials 0.000 description 1
- 235000011130 ammonium sulphate Nutrition 0.000 description 1
- PYMYPHUHKUWMLA-UHFFFAOYSA-N arabinose Natural products OCC(O)C(O)C(O)C=O PYMYPHUHKUWMLA-UHFFFAOYSA-N 0.000 description 1
- SRBFZHDQGSBBOR-UHFFFAOYSA-N beta-D-Pyranose-Lyxose Natural products OC1COC(O)C(O)C1O SRBFZHDQGSBBOR-UHFFFAOYSA-N 0.000 description 1
- 239000003610 charcoal Substances 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 238000002485 combustion reaction Methods 0.000 description 1
- 239000008121 dextrose Substances 0.000 description 1
- 239000003085 diluting agent Substances 0.000 description 1
- AXZAYXJCENRGIM-UHFFFAOYSA-J dipotassium;tetrabromoplatinum(2-) Chemical compound [K+].[K+].[Br-].[Br-].[Br-].[Br-].[Pt+2] AXZAYXJCENRGIM-UHFFFAOYSA-J 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 239000000835 fiber Substances 0.000 description 1
- 229960003711 glyceryl trinitrate Drugs 0.000 description 1
- 238000000227 grinding Methods 0.000 description 1
- 238000010348 incorporation Methods 0.000 description 1
- 239000011777 magnesium Substances 0.000 description 1
- 229910052749 magnesium Inorganic materials 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 229910017464 nitrogen compound Inorganic materials 0.000 description 1
- 150000002830 nitrogen compounds Chemical class 0.000 description 1
- 235000011837 pasties Nutrition 0.000 description 1
- 239000004033 plastic Substances 0.000 description 1
- 235000010333 potassium nitrate Nutrition 0.000 description 1
- 239000004323 potassium nitrate Substances 0.000 description 1
- 229910001487 potassium perchlorate Inorganic materials 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- 229920005989 resin Polymers 0.000 description 1
- 239000011347 resin Substances 0.000 description 1
- 150000003839 salts Chemical class 0.000 description 1
- 239000000779 smoke Substances 0.000 description 1
- 239000011734 sodium Substances 0.000 description 1
- 229910052708 sodium Inorganic materials 0.000 description 1
- 235000010344 sodium nitrate Nutrition 0.000 description 1
- 239000004317 sodium nitrate Substances 0.000 description 1
- VWDWKYIASSYTQR-UHFFFAOYSA-N sodium nitrate Inorganic materials [Na+].[O-][N+]([O-])=O VWDWKYIASSYTQR-UHFFFAOYSA-N 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 235000000346 sugar Nutrition 0.000 description 1
- 150000008163 sugars Chemical class 0.000 description 1
- 229920002258 tannic acid Polymers 0.000 description 1
- LRBQNJMCXXYXIU-NRMVVENXSA-N tannic acid Chemical compound OC1=C(O)C(O)=CC(C(=O)OC=2C(=C(O)C=C(C=2)C(=O)OC[C@@H]2[C@H]([C@H](OC(=O)C=3C=C(OC(=O)C=4C=C(O)C(O)=C(O)C=4)C(O)=C(O)C=3)[C@@H](OC(=O)C=3C=C(OC(=O)C=4C=C(O)C(O)=C(O)C=4)C(O)=C(O)C=3)[C@@H](OC(=O)C=3C=C(OC(=O)C=4C=C(O)C(O)=C(O)C=4)C(O)=C(O)C=3)O2)OC(=O)C=2C=C(OC(=O)C=3C=C(O)C(O)=C(O)C=3)C(O)=C(O)C=2)O)=C1 LRBQNJMCXXYXIU-NRMVVENXSA-N 0.000 description 1
- 229940033123 tannic acid Drugs 0.000 description 1
- 235000015523 tannic acid Nutrition 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C06—EXPLOSIVES; MATCHES
- C06B—EXPLOSIVES OR THERMIC COMPOSITIONS; MANUFACTURE THEREOF; USE OF SINGLE SUBSTANCES AS EXPLOSIVES
- C06B21/00—Apparatus or methods for working-up explosives, e.g. forming, cutting, drying
- C06B21/0033—Shaping the mixture
- C06B21/005—By a process involving melting at least part of the ingredients
Definitions
- It also comprises an explosivejnwhich the ingredients above mentioned are present in substantially homogeneousintermixture, and in which the individual particles of the explosive, in whole or in part, are made up of both ingredients; and it further comprises a process of producing such an explosive5v all as more fully hereinafter set orth'and as claimed; v
- the sulfite liquors used in the paper making process such as calcium, magnesium or sodium bi'sulfite, disintegrate and break up the wood or other fibers, separatingthe cellulose from the non-cellulosic constituents,
- composition of these liquors varies somewhat with the wood treated, with the length and conditions of treatment, and with the sulfite used, the lignin com ounds however, probably in the form of su ionic acid salts, forming the principal constituent of the extractive matter present in the solution.
- the oxidizing agent can be dissolved in the sulfite liquors-"and the liquors evaporated to dryness, or the liquors can be evaporated nearly or completely Specification of Letters Patent,
- a preliminary treatacl'd' present can, for instance,- be neuacidity can be neutralized with lime and insoluble lime compounds removed.
- the liquors can be concentrated or even evaporated to dryness, and the concentrated liquor, or plastic or solid. mass used for making the novel explosives.
- the sulfite liquors are evapo- .mixing can then be efi'ected the mixing machine. It .is, however, in general more with the waste sulfite liquors while still in solution or while there is still enough liquor or liquid present to make the mixing a Wet,
- the dry mixing process offers the advantage that the constituents of the sulfite waste liquors when evaporated. to dryness become much less soluble, so that the mixture partalres more of the nature of a mixture of the oxidizing agent with insoluble ingredients.
- geously liquid or when can be further treated to give to it the deto the wet process of the present invention can be eiiected in various ways. It is usually suiiicient merely to dissolve the oxidizing agent in the liquor, and evaporate to dryness. Such evaporation is advanta effected with stirring to promote homogeneity. Again the solution can be run in theform of a thin stream on to rollers internally heated-by steam to 100 or above by means oii which practically instantaneous evaporation can be eiiected. The evaporated ribbon like inassis scraped oft the rollers by scrapers, or other appliances.
- Such heated rollers can be arranged in a vacuum chamber and the evaporation or drying effected at a correspondingly lower temperature.
- the temperature should be kept below that at which the am: -monium compounds, are decomposed or volatilized.
- the evaporation of the waste sulfite liquors tends to make the wood fiber constituents contained in them lesssoluble, so that the final products are insoluble or relatively much use soluble than before evaporation.
- the explosive after removal of the compounded in a dry state,
- sired shape or consistency can be used as an exploslv either alone or cornblncd with other e 'ploslve ingredients, or
- ammonium nitrate'explosives of the r'esentwtion can be detonated with primers and are very'efiective. Even when diluted by the addition ofappreciable amounts of inert substances they can still be reliably detonated 'and 'possess high explosive power.
- the addition of up to 30% of such an inert material as sulfate of sodium can be made,
- Example 1 parts of nitrate of ammonium are dissolved in waste sulfite liquors containing 15 parts of dry wood fiber constituents. The liquors are then evaporated to dryness with stirring, or by running the liquid on steam heated rollers heated to 100 or above as already described. The sulfite liquors used may be in their diluted condition, or partially evaporated. Again the sulfite liquors can be evaporated to dryness and the dried material and the oxygen carrier mixed in a mixing machine; or the sulfite waste may be evaporated to a thick but still liquid or pasty consistency and the alkali nitrate incorporated therewith.
- Example 2 60 parts of nitrate of ammonia and 30 parts of sulfate of sodium are dissolved in waste sulfite liquors containing 10 parts of wood fiber constituents, and the liquors are evaporated to dryness as allready described.
- ammonium nitrate instead of the ammonium nitrate of the foregoing examples,sodium or potassium nitrate, or other oxidizing agent or agents can be used, such as potassium perchlorate, etc.
- non-cellulosic wood fiber constituents is used in the present specification and claims to indicate those ingredients of wood and similar. cellulosic material from which the paper stock or cellulose has been entirely or substantially, removed by such processes as those employed in paper making, the cellulose itself constituting the pulp or paper stock.
- sulfite Waste constituents is similarly used, but with a. more specific'meaning, to indicate those ingredients of wood and similar material which are found in solution in the waste sulfite liquors resulting from the sulfite process 0]": pulp treatment, and from which the pulp or. cellulosic material itself has been separated.
- An expiasive comprising ammonium nitrate and suifite "waste constituents, in which explosive the individual particles include both ingredients.
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Paper (AREA)
Description
, No Drawing.
mam onnion rnrrz masonic, on" LnnwmsnArEN-on rnn-nnmn, ennmany.
SULFITE-WASTE EXPLOSIVE.
1&56 366.
T 0 all whom it may concern:
Be itknown that I, FRITZ RAscHIc, doctor of philosophy, chemist, a citizen of the Gerand sulfite-waste constituents.
It also comprises an explosivejnwhich the ingredients above mentioned are present in substantially homogeneousintermixture, and in which the individual particles of the explosive, in whole or in part, are made up of both ingredients; and it further comprises a process of producing such an explosive5v all as more fully hereinafter set orth'and as claimed; v In the manufacture'oi paper or of paper pulp by thesulfite process ap roximately one-halfofthe Wood or other ce lulosic material treated 'isipresent in the waste liquors, commonly known as waste sulfiteliquors. The sulfite liquors used in the paper making process, such as calcium, magnesium or sodium bi'sulfite, disintegrate and break up the wood or other fibers, separatingthe cellulose from the non-cellulosic constituents,
' and dissolving the lignin or lignone and other soluble non-cellulosic constituents. Among the products present in this sulfite solution are dextrose and various other sugars,.xylose, aceticaci'd, tannic acid, nitrogen-compounds, resins, etc, as well as the so-called alkali .orearth alkali lignin-sulfonates, which last named products are the principal prod cts of the reaction of the sulfite upon the wood-fibers treated. The composition of these liquors varies somewhat with the wood treated, with the length and conditions of treatment, and with the sulfite used, the lignin com ounds however, probably in the form of su ionic acid salts, forming the principal constituent of the extractive matter present in the solution.
In making the novel explosives of the present invention the oxidizing agent can be dissolved in the sulfite liquors-"and the liquors evaporated to dryness, or the liquors can be evaporated nearly or completely Specification of Letters Patent,
Application filed April 11, 1912. Serial No. 690,184;
Patented Mar. s, 1913,
to, dryness and the oxidizin mately intermixed with the' l ably or strongly acid, to neutralize or other wise sub ect them to a preliminary treatacl'd' present can, for instance,- be neuacidity can be neutralized with lime and insoluble lime compounds removed. The liquors can be concentrated or even evaporated to dryness, and the concentrated liquor, or plastic or solid. mass used for making the novel explosives.
In making the new explosives by the dry mixing method the sulfite liquors are evapo- .mixing can then be efi'ected the mixing machine. It .is, however, in general more with the waste sulfite liquors while still in solution or while there is still enough liquor or liquid present to make the mixing a Wet,
intimacy of incorporationof the ingredients is thus possible, and a homogeneity of prod tain with the dry mixing process. For, since the ingredients when in solution are capable of greater interpenetration, the re-. sulting product obtained from such wet nearly homogeneous intermixture, and the up! in whole or in part of both ingredients. '1 e homogeneous nature of the product thus obtainable enables substantially com.-
plete combustion to take place, and as a result the-formation of smoke is minimized or entirely avoided. The dry mixing process, however, offers the advantage that the constituents of the sulfite waste liquors when evaporated. to dryness become much less soluble, so that the mixture partalres more of the nature of a mixture of the oxidizing agent with insoluble ingredients.
The incorporation or intermixture of the oxidizing agent and the wood fiber constituents oi the waste sufite liquors, according agent inti-" ry material." It is frequently advantageous, especially where the sulfite waste liquors are appreoa l" ment or concentration before using- The rated to dryness, and advantageously given a preliminary grinding and breaking up before mixing with the oxidizing agent. The
advantageous to mix the oxidizing agent uct obtainable, which it is impossible to ob-' mixing contains the ingredients ina more particles of the explosive obtained are made t-ralized with ammonia, the calcium. pre i. cipitated with ammonium sulfate, and the" calcium sulfate filtered off; or again the 'as dsitinguished from a dry, mixing. An
. geously liquid, or when can be further treated to give to it the deto the wet process of the present invention can be eiiected in various ways. It is usually suiiicient merely to dissolve the oxidizing agent in the liquor, and evaporate to dryness. Such evaporation is advanta effected with stirring to promote homogeneity. Again the solution can be run in theform of a thin stream on to rollers internally heated-by steam to 100 or above by means oii which practically instantaneous evaporation can be eiiected. The evaporated ribbon like inassis scraped oft the rollers by scrapers, or other appliances. Again such heated rollers can be arranged in a vacuum chamber and the evaporation or drying effected at a correspondingly lower temperature. In the case of the ammonium nitrate explosives the temperatureshould be kept below that at which the am: -monium compounds, are decomposed or volatilized. The evaporation of the waste sulfite liquors tends to make the wood fiber constituents contained in them lesssoluble, so that the final products are insoluble or relatively much use soluble than before evaporation. The explosive, after removal of the compounded in a dry state,
sired shape or consistency, and it can be used as an exploslv either alone or cornblncd with other e 'ploslve ingredients, or
with modifying ingredients or diluents' Small amounts of such materials as vascline, 35,
wax, etc. can be'mixed withthe explosive, or film-torming solutions can be used to intermix or coat the particles of the explosive. V
k The explosives obtainable from the sulfite waste constituents a d ammonium nitrate as the oxygen carrier 'orm ammonium nitrate explosives with many valuable properties and uses not inherent in the old ammonium nitrate explosives made by mixing ammonium nitrate with such combustible substances as charcoal powder, cornmeal, etc.
Such old explosives are not reliable when detonated wlt-h primers, it being necessary to add thereto highly explosive substances such as trinitrotoluol or nitroglycerin, etc.
The ammonium nitrate'explosives of the r'esentwtion, on the other hand, can be detonated with primers and are very'efiective. Even when diluted by the addition ofappreciable amounts of inert substances they can still be reliably detonated 'and 'possess high explosive power. The addition of up to 30% of such an inert material as sulfate of sodium can be made,
' and reliable andeflicient explosives still obtained.
The present invention, which is of general application, is further illustrated and exemplified by the following specific embodiments of its application.
Example 1: parts of nitrate of ammonium are dissolved in waste sulfite liquors containing 15 parts of dry wood fiber constituents. The liquors are then evaporated to dryness with stirring, or by running the liquid on steam heated rollers heated to 100 or above as already described. The sulfite liquors used may be in their diluted condition, or partially evaporated. Again the sulfite liquors can be evaporated to dryness and the dried material and the oxygen carrier mixed in a mixing machine; or the sulfite waste may be evaporated to a thick but still liquid or pasty consistency and the alkali nitrate incorporated therewith.
Example 2 60 parts of nitrate of ammonia and 30 parts of sulfate of sodium are dissolved in waste sulfite liquors containing 10 parts of wood fiber constituents, and the liquors are evaporated to dryness as allready described.
Instead of the ammonium nitrate of the foregoing examples,sodium or potassium nitrate, or other oxidizing agent or agents can be used, such as potassium perchlorate, etc.
Sulfite waste liquors made from other cellulosic material than wood can'be used in a similar manner. 1
Variations and modifications can be made in the processes and roducts above described without departing from the spirit and scope of the invention, and all such variations and modifications are embraced within the invention as set forth in the accompanying claims.
The term non-cellulosic wood fiber constituents is used in the present specification and claims to indicate those ingredients of wood and similar. cellulosic material from which the paper stock or cellulose has been entirely or substantially, removed by such processes as those employed in paper making, the cellulose itself constituting the pulp or paper stock. The term sulfite Waste constituents is similarly used, but with a. more specific'meaning, to indicate those ingredients of wood and similar material which are found in solution in the waste sulfite liquors resulting from the sulfite process 0]": pulp treatment, and from which the pulp or. cellulosic material itself has been separated.
I claim:
1. The process of producing an explosive which comprises mtcrmixing an oxidizing agent with sulfite waste liquors, and evapo producing an inierinixing ammoni n'asie constituenis in in.
and evaporating ii liqui i, e
comprising an oxidizing d 5. An efizpiosiva iosic wood fiber COIXStihP 11;; an oxidizing wants f ceniprising an oxidizing v-xnsie coustitunts in which 1 parizicies incmcie nitrate and sniiite Waste constituents.
10. An expiasive comprising ammonium nitrate and suifite "waste constituents, in which explosive the individual particles include both ingredients.
In testimony whereof I have hereunto set my hand in the presence of two SUi)C1'ii)i1lg witnesses. v
FRITZ RASCH G; Witnesses:
RICHARD Rncnnn, Jonnrmns DEUSGHEL.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US69018412A US1056366A (en) | 1912-04-11 | 1912-04-11 | Sulfite-waste explosive. |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US69018412A US1056366A (en) | 1912-04-11 | 1912-04-11 | Sulfite-waste explosive. |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US1056366A true US1056366A (en) | 1913-03-18 |
Family
ID=3124620
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US69018412A Expired - Lifetime US1056366A (en) | 1912-04-11 | 1912-04-11 | Sulfite-waste explosive. |
Country Status (1)
| Country | Link |
|---|---|
| US (1) | US1056366A (en) |
-
1912
- 1912-04-11 US US69018412A patent/US1056366A/en not_active Expired - Lifetime
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