US2805117A - Method of preparing a tanning composition comprising basic chromic sulfate - Google Patents

Method of preparing a tanning composition comprising basic chromic sulfate Download PDF

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US2805117A
US2805117A US378994A US37899453A US2805117A US 2805117 A US2805117 A US 2805117A US 378994 A US378994 A US 378994A US 37899453 A US37899453 A US 37899453A US 2805117 A US2805117 A US 2805117A
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tanning
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Tom S Perrin
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Diamond Shamrock Corp
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Diamond Alkali Co
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    • CCHEMISTRY; METALLURGY
    • C14SKINS; HIDES; PELTS; LEATHER
    • C14CCHEMICAL TREATMENT OF HIDES, SKINS OR LEATHER, e.g. TANNING, IMPREGNATING, FINISHING; APPARATUS THEREFOR; COMPOSITIONS FOR TANNING
    • C14C3/00Tanning; Compositions for tanning
    • C14C3/02Chemical tanning
    • C14C3/04Mineral tanning
    • C14C3/06Mineral tanning using chromium compounds

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  • This invention relates to an improved chromium-containing tanning substance and to methods of preparing the same.
  • chromium in its trivalent state probably in the form of the oxide, has a fixing or tanning action on the hide or skin substances which are subject to putrescence, and upon the chromium so acting on such substances, the hide or skin is tanned and becomes leather.
  • the art of applying chromium-containing materials to hides or skins to make leather is quite old and started with the use of highly acid compounds of chromium which were subsequently neutralized in the hide or skin by addition thereto of basic materials.
  • dichromate could be used as a source material for the one-bath chrome tan and could be placed in proper trivalent basic condition by reduction with sundry reducing agents, of which sugar and sulfur dioxide are exemplary and are commercially practiced.
  • a dichromate solution is treated with a reducing agent, such as sugar, and upon the completion of the reduction, the solution contains approximately 25% of chromium as CH0: and considerable inert salt of sodium with the acid used in the process of manufacture, usually sodium sulfate, which material has no value except as an inert in the tanning salt.
  • the solution as prepared is suitably dried either by spray-drying or other conventional drying means and, as such, is ready for shipping to a tanner, who makes up a tanning solution from it as needed.
  • the disadvam tages previously existing in one-bath chrome tan materials have been removed by modification in the procedures employed to obtain the tanning salt.
  • the crude chromic acid crystals obtained by the reaction of saturated commercial dichromate solutions with sulfuric acid produces a solution which, upon reduction of the hexavalent chromium and subsequent drying of the solution such as by spray drying, is materially higher in chronic content and, accordingly, lower in sodium sulfate content and, moreover, is substantially entirely free of vanadium impurity since the vanadium impurity goes out with the mother liquor from the crystallization of chromic acid.
  • chrometanning salt which is higher in chromium content and lower in sodium sulfate permits the tanner, upon working up his tanning solutions, to use less of the tanning compound for a given tanning job and still have the same amount of chrome concentration in his tanning solutions.
  • Another advantage of the present invention lies in the fact that the crude material obtained by the reaction of a concentrated commercial dischromate solution with sulfuric acid, may itself be forwarded to a tanner and reduced by the tanner in his own tannery for immediate use as a chrome-tanning material, thus eliminating the drying step.
  • no waste material, such as sodium sulfate need be shipped, and the freight charges are, ac ⁇ cordingly, minimized, especially where the tanner is operating on a large scale and can aifordto take substantial quantities of the crude chromic acid material.
  • a saturated solution of 'sodiurn'dichromate (70%) is combined with sulfuric acid .in a suitablereactor.
  • the concentration of the sulfuric acid may vary between 78% H2804 and 20% oleum (104.5% H2804), preferablyabout HzSO4.
  • the addition of the concentrated acid to the saturated sodium dichromate solution is suitably controlled'to maintain the temperature in the reactor within the range of 50 -to 65" C.
  • the amountof the acid employed may varywithin the range of 3 to 4.5 moles vof -H2S O4.pe'r mol 'of sodium dichromate. dihydrate, but it is of particular-advantage in preparing a tanningsalt inaccordance with the method of the present inventioii, to minimize Patented Sept; 3, .1957
  • the ideal ratio is of the order of 3.5 moles of H2804 per mol ofdichroniate, and this is preferred.
  • the 'reaction'niixture may be maintained'in the reactor-for a period .of at least one-quarter hourrto insure substantially complete reaction to chromic anhydride; Retention times longer than this are not harmful since the only effect obtained'is to contaminate the material with reduced chrome. 'As all the hexavalent chrome is to ,be reducedrin the next step of the process, no harm is done by further holding the material in the reactor; 7
  • the reaction mass comprising a magma of chromic acidcrystals and mother liquor may be passedto'a suitable means for separation of the 'chromic acid crystals from ,the'mother liquor, for example, a centrifuge.
  • suitable means for separation of the 'chromic acid crystals from ,the'mother liquor for example, a centrifuge.
  • the temperature maintained in the separation means, such as a centrifuge suitable varies between 50 and 65 C., it being noted that it is preferable in the case of preparationof the tanning salt of this invention, to maintain the temperature at least above 50 C. to avoid overprecipitation of sodium acid sulfate with the chromic acid.
  • washing of the crystals in the centrifuge may be employed if desired, but no special advantage accrues therefrom as the subsequent steps of the process, i. e., acidification and reduction substantially preclude any advantage of washing at this point.
  • the material to be processed in accordance with the remaining steps of the method of this invention is derived as a side stream from a-chromic acid manufacturing process in which the main stream comprises highly purified chromic acid, then the material at this point may be a washed, or otherwise worked-up, crude chromic acid crystal mass. 'Such working-up may include washing of the crude crystals as aforesaid or actual addition of sodium bichromate dihydrate as crystals or as liquor say in the form of a 70% solution.
  • the intermediate product comprises a combination of chromic acid, sodium acid sulfate, and water, the chromic acid normally ranging between about 80%-95%.
  • a material having as little as 3% of bisulfate is obtained.
  • This ma: terial is a crystalline, readily-soluble substance, the crystal size depending upon the method of precipitation but being of the order of that of common granulated sugar. If the material is to be processed immediately into a tanning salt, then no drying step is necessary at this point to remove the residual water; in some instances, if the material is not to be kept for a too great period of time without further processing, drying may be dispensed with.
  • the above-described product is, when it is desired to prepare the tanning salt,'dissolved injwater, to. produce ,a substantially saturated solution thereof.
  • Other substances may be added to the solution, if desired, such as aluminum sulfate for its known'func tion'intanning.
  • Sulfuric acid is addedtothe system to adjust thepHto below" 1.0 and the chrome reduced by I any convenient reducing agent, of which sulfur dioxide or sundry organic materials, such as sugar, are exemplary.
  • the pH of the solution may suitably be adjusted to produce the desired basicity of the tanning salt, suitably in the range of pH 2.75-3.5, and then the solution may be dried by any desired means, such as application of heat thereto, spray-drying, and the like.
  • the final product may contain of the order of or more chromium as Cir-203, as compared with a maximum of about 25% of chromium as. CrsOs, which can be obtained by preparing a similar tanning salt from sodium dichromate liquor by prior art practice.
  • the diiference is more substantial than actually would seem apparent from the figures involved, since in the prior art tanning salt, the remainder of the material is inert sodium sulfate which, as noted above, has no tanning. value per se, but which must nevertheless be'shipped to the point of use as 'a part of the salt.
  • the additional amount of chromium in the tanning salt admits of shipping of less sodium sulfate and, moreover, admits of use of less tanning salt on actual ,1 point of use to obtain the same chromium concentration in a, tanning bath.
  • a tanner is prepared to use the material, it is simply dissolved in water to the desired concentration and employed in a well-known manner for tanning skins.
  • Example II corn. sugar syrup, the temperature being maintained by externalcooling within therange of "'-80. C. and agitation being continuous during the reduction.
  • the pH at this pointdafter reduction is found to be complete 'andis' below 1;0, whereupon 6.5 gms. of sodium carbonate'solution'are added to bring'the pH to 3.3.
  • the material isplaced in an evaporating dish and dried in an oven over-night, whereupon a' dried tanning salt is obtained having 32.89% of, chromium, calculated as CrzOgyand, 0.018% of'vanadium, calculated as V205, and but' 4.97% ofNaz SOo Example II
  • a comparable run is made from the same sample of liquor'as the starting material of Example I.
  • S02 when for reasonsof supply,or other reasons, it is desired to employ some S02 in the initial phase ofthe reduction but not to complete the reduction with S02 especially in view of theunreasonably large and unwanted amount of sulfate therebyproduced in the finallcompositions .
  • a desired amount of S02. need be used such as that which is equivalent to production of basic chromic sulfate in the system, whereupon an organic reducing agent (such as sugar or any organic substance having reducing properties, viz., propanol), may be employed to complete the reduction.
  • an organic reducing agent such as sugar or any organic substance having reducing properties, viz., propanol
  • the method of preparing a tanning composition comprising basic chromium sulfate, which includes the steps of providing a substantially saturated solution of an alkali metal dichromate, adding to said solution sul furic acid in an amount of from 3 to 4.5 moles of HzSO4 per mol of alkali metal dichromate, said acid having a concentration substantially within the range of 78%- 104.5% H2SO4 by weight, maintaining the temperature of the mixture of said acid and said solution substantially within the range of 50-65 C.

Description

p 3, 1957 T. s. PERRIN 2,805,117.
METHOD OF PREPARING A TANNING COMPOSITION COMPRISING BASIC CHROMIC SULFATE Filed Sept. 8, 1953 uq vcr O-,- 2H2O 70% LIQUOR REACTOR CRYSTALS PLUS MOTHER LIQUOR CENTRIFUGE I MOTHER LIQUOR v CRUDE 0'0 CRYSTALS' DISSOLVE- ADD IN ORDER:
l.H SO TO pH w ZREDUCING AGENT (STOICHIOMETRIC AMOUNT) a. BASE TO pH 225-35 REDUCED CHROMIU M SOLUTION DRY I TANNING SALT I TOM- s. PERRIN ATTORNEY INVENTOR United States Patent fl METHOD OF PREPARING A TANNING COMPOSI- TION COMPRISING BASIC CHROMIC SULFATE Tom S. Perrin, Painesville, Ohio, assignor to Diamond Alkali Company, Cleveland, Ohio, a corporation of Delaware Application September 8, 1953, SerialNo. 378,994
3 Claims. (Cl. 8-94.27)
This invention relates to an improved chromium-containing tanning substance and to methods of preparing the same.
It has long been known that chromium in its trivalent state, probably in the form of the oxide, has a fixing or tanning action on the hide or skin substances which are subject to putrescence, and upon the chromium so acting on such substances, the hide or skin is tanned and becomes leather. The art of applying chromium-containing materials to hides or skins to make leather is quite old and started with the use of highly acid compounds of chromium which were subsequently neutralized in the hide or skin by addition thereto of basic materials. It was early found, however, that damage was done to the skin by the highly acid compounds, such as chromic acid, and that the tannage could, moreover, be accomplished more efficiently and better tannage obtained with a single treatment employing a basic chromiumsalt or one-bath tan. This was taught in Dennis Patent No. 495,028, which patent established the basic process in the art which is still employed today.
Following the development of the so-called one-bath chrome tan, it was soon found, upon the development of the dichromate industry, that dichromate could be used as a source material for the one-bath chrome tan and could be placed in proper trivalent basic condition by reduction with sundry reducing agents, of which sugar and sulfur dioxide are exemplary and are commercially practiced. In accordance, therefore, with prior art methods of making one-bath chrome tans, a dichromate solution is treated with a reducing agent, such as sugar, and upon the completion of the reduction, the solution contains approximately 25% of chromium as CH0: and considerable inert salt of sodium with the acid used in the process of manufacture, usually sodium sulfate, which material has no value except as an inert in the tanning salt. The solution as prepared is suitably dried either by spray-drying or other conventional drying means and, as such, is ready for shipping to a tanner, who makes up a tanning solution from it as needed.
The large amount of sodium sulfate which must be shipped with the reduced chrome has heretofore been regarded as a necessary evil, in that there was no feasible way of producing one-bath chrome tans from "sodium dichromate, the commonest source of chromium for the purpose, without the accompanying sodium sulfate; It is true, of course, that some salt of some kind, is preferably present with the tanning material when the same is in contact with a skin to be tanned. Such salt aids in preventing the skin absorbing an undesired amount of water during tanning. It has no tanning functionper se. The cheapest salt for the purpose is sodium chloride which may suitably be combined with the tanning solution when it is made up. The prior art was forced to the expedient of employing the already present sodium sulfate as the tanning compound could not be obtained without it.
A further disadvantage of the material ,pre'pared'in accordance with prior art procedures is that vanadium,
streaky cast to the leather and renders the same un'-' merchantable In accordance with the present invention, the disadvam tages previously existing in one-bath chrome tan materials have been removed by modification in the procedures employed to obtain the tanning salt. Thus, rather than employing expensive purified sodium dichromate crystals or previously purified solutions of dichromate as the source of chrome in the tanning salt, it has now been found that the crude chromic acid crystals obtained by the reaction of saturated commercial dichromate solutions with sulfuric acid, produces a solution which, upon reduction of the hexavalent chromium and subsequent drying of the solution such as by spray drying, is materially higher in chronic content and, accordingly, lower in sodium sulfate content and, moreover, is substantially entirely free of vanadium impurity since the vanadium impurity goes out with the mother liquor from the crystallization of chromic acid. The provision of a chrometanning salt which is higher in chromium content and lower in sodium sulfate permits the tanner, upon working up his tanning solutions, to use less of the tanning compound for a given tanning job and still have the same amount of chrome concentration in his tanning solutions. The savings in shipment costs and the like, therefore, are quite substantial.
Another advantage of the present invention lies in the fact that the crude material obtained by the reaction of a concentrated commercial dischromate solution with sulfuric acid, may itself be forwarded to a tanner and reduced by the tanner in his own tannery for immediate use as a chrome-tanning material, thus eliminating the drying step. In such case, no waste material, such as sodium sulfate, need be shipped, and the freight charges are, ac} cordingly, minimized, especially where the tanner is operating on a large scale and can aifordto take substantial quantities of the crude chromic acid material.
The present invention may be more fully understood from the flow-sheet attached hereto and from the follow-' ing descriptive statement respecting the flow-sheet:
, Initially, it is noted that while the flow-sheet sets forth the subject matter'hereof in the terms of employing commercial (70%) sodium dichromate solution as a starting material, the principles of the present invention are applicable todichromates of other alkali metals, such .as lithium, potassium, rubidium, and cesium, though none of theseis normally employed for tanning purposes, with the possible exception of potassium, since the sodium salt is the least expensive and the inerts ultimately in the tanning salt, being in the form of sodium salts, are of no significance to the tanning process as such.
In the 'flow=sheet, it will be noted that a saturated solution of 'sodiurn'dichromate (70%) is combined with sulfuric acid .in a suitablereactor. The concentration of the sulfuric acid may vary between 78% H2804 and 20% oleum (104.5% H2804), preferablyabout HzSO4. The addition of the concentrated acid to the saturated sodium dichromate solution is suitably controlled'to maintain the temperature in the reactor within the range of 50 -to 65" C. The amountof the acid employedmay varywithin the range of 3 to 4.5 moles vof -H2S O4.pe'r mol 'of sodium dichromate. dihydrate, but it is of particular-advantage in preparing a tanningsalt inaccordance with the method of the present inventioii, to minimize Patented Sept; 3, .1957
tained and to obtain as much chromic acid in the crystallized material as is possible. In order to do this, the ideal ratio is of the order of 3.5 moles of H2804 per mol ofdichroniate, and this is preferred.
:QThe 'reaction'niixture may be maintained'in the reactor-for a period .of at least one-quarter hourrto insure substantially complete reaction to chromic anhydride; Retention times longer than this are not harmful since the only effect obtained'is to contaminate the material with reduced chrome. 'As all the hexavalent chrome is to ,be reducedrin the next step of the process, no harm is done by further holding the material in the reactor; 7
The reaction mass comprising a magma of chromic acidcrystals and mother liquor may be passedto'a suitable means for separation of the 'chromic acid crystals from ,the'mother liquor, for example, a centrifuge. The temperature maintained in the separation means, such as a centrifuge, suitable varies between 50 and 65 C., it being noted that it is preferable in the case of preparationof the tanning salt of this invention, to maintain the temperature at least above 50 C. to avoid overprecipitation of sodium acid sulfate with the chromic acid.
Washing of the crystals in the centrifuge may be employed if desired, but no special advantage accrues therefrom as the subsequent steps of the process, i. e., acidification and reduction substantially preclude any advantage of washing at this point. When the material to be processed in accordance with the remaining steps of the method of this invention, is derived as a side stream from a-chromic acid manufacturing process in which the main stream comprises highly purified chromic acid, then the material at this point may be a washed, or otherwise worked-up, crude chromic acid crystal mass. 'Such working-up may include washing of the crude crystals as aforesaid or actual addition of sodium bichromate dihydrate as crystals or as liquor say in the form of a 70% solution. No advantage accrues to this process by such treatment, but the economic burden of processing a separate stream solely for the raw material to be worked-up into a tanning compound in accordance herewith, may well outweigh the minor disadvantages and increase in cost of the tanning compound which arises from processing a. somewhat more elaborately preparedcrude chromic acid crystal mass. It is, however, the preference-of this invention to separate crystals from the mother liquor without further work-up. At this point in the process, the intermediate product comprises a combination of chromic acid, sodium acid sulfate, and water, the chromic acid normally ranging between about 80%-95%. Suitably, by maintaining an acidzdichromate ratio of 3.5 :1 and the holding temperature of centrifuging in excess of 50 C., a material having as little as 3% of bisulfate is obtained. This ma: terial is a crystalline, readily-soluble substance, the crystal size depending upon the method of precipitation but being of the order of that of common granulated sugar. If the material is to be processed immediately into a tanning salt, then no drying step is necessary at this point to remove the residual water; in some instances, if the material is not to be kept for a too great period of time without further processing, drying may be dispensed with. here, however, it is intended to ship the material to a difierent geographic point for further processing into a tanning salt, it is preferable to remove the water therefrom prior to packaging, which removal may. easily be accomplished by heating the substance to 100 C. for a relatively short period of time. 7
Whether the tanning salt. is to be prepared immediately or in the future, the above-described product is, when it is desired to prepare the tanning salt,'dissolved injwater, to. produce ,a substantially saturated solution thereof. Other substances may be added to the solution, if desired, such as aluminum sulfate for its known'func tion'intanning. Sulfuric acid is addedtothe system to adjust thepHto below" 1.0 and the chrome reduced by I any convenient reducing agent, of which sulfur dioxide or sundry organic materials, such as sugar, are exemplary. Following the reduction of the hexavalent chromium to trivalent chromium, the pH of the solution may suitably be adjusted to produce the desired basicity of the tanning salt, suitably in the range of pH 2.75-3.5, and then the solution may be dried by any desired means, such as application of heat thereto, spray-drying, and the like.
In the dried form, the final product may contain of the order of or more chromium as Cir-203, as compared with a maximum of about 25% of chromium as. CrsOs, which can be obtained by preparing a similar tanning salt from sodium dichromate liquor by prior art practice. The diiference is more substantial than actually would seem apparent from the figures involved, since in the prior art tanning salt, the remainder of the material is inert sodium sulfate which, as noted above, has no tanning. value per se, but which must nevertheless be'shipped to the point of use as 'a part of the salt. In the present instance, the additional amount of chromium in the tanning salt admits of shipping of less sodium sulfate and, moreover, admits of use of less tanning salt on actual ,1 point of use to obtain the same chromium concentration in a, tanning bath. When a tanner is prepared to use the material, it is simply dissolved in water to the desired concentration and employed in a well-known manner for tanning skins.
.ln, order that those skilled in the art may more fully understand the. method of the present invention, the following specific examples are offered:
A thereto. The reduction is carried on with 7.84 gms. of
corn. sugar syrup, the temperature being maintained by externalcooling within therange of "'-80. C. and agitation being continuous during the reduction. The pH at this pointdafter reduction is found to be complete 'andis' below 1;0, whereupon 6.5 gms. of sodium carbonate'solution'are added to bring'the pH to 3.3. The material isplaced in an evaporating dish and dried in an oven over-night, whereupon a' dried tanning salt is obtained having 32.89% of, chromium, calculated as CrzOgyand, 0.018% of'vanadium, calculated as V205, and but' 4.97% ofNaz SOo Example II A comparable run is made from the same sample of liquor'as the starting material of Example I. This run is in accordance with the best'techniques known for reducing dichromate prior to this invention; Thus, 25 gms. of H2504 are combined with 35.8 gms. of NazCrzOmZHzO liquor and reduced with 8.9 gms. of corn sugar syrup." 'The pH is adjusted to 3.2 and the solution spray-dried as before. A tanning salt containing 24.66% 'of chromium, as G203, and 0.064% of vanadium; as V205, and 25.47% of NasSOr is produced. While-reduction by both organic and inorganic reducing agents has been described, it is also feasible in some instances to employ-both types of reducing agents in the samereduction batch. This is especially true. when for reasonsof supply,or other reasons, it is desired to employ some S02 in the initial phase ofthe reduction but not to complete the reduction with S02 especially in view of theunreasonably large and unwanted amount of sulfate therebyproduced in the finallcompositions .In this case, only a desired amount of S02. need be used such as that which is equivalent to production of basic chromic sulfate in the system, whereupon an organic reducing agent (such as sugar or any organic substance having reducing properties, viz., propanol), may be employed to complete the reduction.
This is a continuation-in-part of application Ser. No. 319,361, filed November 7, 1952, now abandoned.
While there have been described various embodiments of the invention, the methods described are not intended to be understood as limiting the scope of the invention as it is realized that changes therewithin are possible and it is further intended that each element recited in any of the following claims is to be understood as referring to all equivalent elements for accomplishing substantially the same results in substantially the same or equivalent manner, it being intended to cover the invention broadly in whatever form its principle may be utilized.
What is claimed is:
1. The method of preparing a tanning composition comprising basic chromium sulfate, which includes the steps of providing a substantially saturated solution of an alkali metal dichromate, adding to said solution sul furic acid in an amount of from 3 to 4.5 moles of HzSO4 per mol of alkali metal dichromate, said acid having a concentration substantially within the range of 78%- 104.5% H2SO4 by weight, maintaining the temperature of the mixture of said acid and said solution substantially within the range of 50-65 C. until CrOs crystals precipitate, separating said CI'Os crystals from the mother liquor so as to leave a comparatively small amount of the mother liquor adhering to said crystals, dissolving said crystals and mother liquor in water to form a solution containing chromic acid, adjusting the pH of the 6 chromic acid solution with a strong mineral acid to a value below 1.0, reducing the hexavalent chromium of said solution to trivalent chromium by applying an aqueous solution of a chemical reducing agent, adjusting the pH of said trivalent chromium solution with an aqueous alkaline solution to a point substantially within the range of 2.753.5, drying the aforesaid solution and recovering References Cited in the file of this patent UNITED STATES PATENTS 556,325 Sadtler Mar. 10, 1896 688,294 Carmichael Dec. 10, 1901 1,872,588 Hines Aug. 16, 1932 2,034,256 Vetter Mar. 17, 1936 2,110,961 Merritt Mar. 15, 1938 2,178,874 Hervey Nov. 7, 1939 2,335,365 Smith Nov. 30, 1943 FOREIGN PATENTS 586,874 Great Britain Apr. 3, 1947

Claims (1)

1. THE METHOD OF PREPARING A TANNING COMPOSITION COMPRISING BASIC CHROMIUM SULFATE, WHICH INCLUDES THE STEPS OF PROVIDING A SUBSTANTIALLY SATURATED SOLUTION OF AN ALKALI METAL DICHROMATE, ADDING TO SAID SOLUTION SULFURIC ACID IN AN AMOUNT OF FROM 3 TO 4.5 MOLES OF H2SO4 PER MOL OF ALKALI METAL DICHROMATE, SAID ACID HAVING A CONCENTRATION SUBSTANTIALLY WITHIN THE RANGE OF 78% 104.5% H2SO4 BY WEIGHT, MAINTAINING THE TEMPERATURE OF THE MIXTURE OF SAID ACID AND SAID SOLUTION SUBSTANTIALLY WITHIN THE RANGE OF 50-65*C. UNTIL CRO3 CRYSTALS PRECIPITATE, SEPARATING SAID CRO3 CRYSTALS FROM THE MOTHER LIQUOR SO AS TO LEAVE A COMPARATIVELY SMALL AMOUNT OF THE MOTHER LIQUOR ADHERING TO SAID CRYSTALS, DISSOLVING
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Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3081142A (en) * 1960-03-12 1963-03-12 Mezei Ernesto Vegetable one-bath pretanning process
US3927966A (en) * 1973-11-07 1975-12-23 Schill & Seilacher Process of producing a fatliquoring chrome tanning agent, composition containing same and method of using same

Citations (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US556325A (en) * 1896-03-10 Process of making leather
US688294A (en) * 1896-12-14 1901-12-10 Henry Carmichael Process of tanning hides or skins.
US1872588A (en) * 1929-04-15 1932-08-16 Harshaw Chem Corp Manufacture of chromium trioxide
US2034256A (en) * 1930-05-27 1936-03-17 Natural Products Refining Co Process for producing chromic acid
US2110961A (en) * 1936-04-10 1938-03-15 Tanning Process Co Tanning of hides and skins
US2178874A (en) * 1937-05-06 1939-11-07 Little Inc A Process of preparing tanning material and by-products derived therefrom
US2335365A (en) * 1941-08-14 1943-11-30 Carbide & Carbon Chem Corp Production of chromium trioxide
GB586874A (en) * 1944-06-21 1947-04-03 William Walker And Sons Ltd Improvements in the manufacture of heat-resistant and durable leathers and tanning agents therefor

Patent Citations (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US556325A (en) * 1896-03-10 Process of making leather
US688294A (en) * 1896-12-14 1901-12-10 Henry Carmichael Process of tanning hides or skins.
US1872588A (en) * 1929-04-15 1932-08-16 Harshaw Chem Corp Manufacture of chromium trioxide
US2034256A (en) * 1930-05-27 1936-03-17 Natural Products Refining Co Process for producing chromic acid
US2110961A (en) * 1936-04-10 1938-03-15 Tanning Process Co Tanning of hides and skins
US2178874A (en) * 1937-05-06 1939-11-07 Little Inc A Process of preparing tanning material and by-products derived therefrom
US2335365A (en) * 1941-08-14 1943-11-30 Carbide & Carbon Chem Corp Production of chromium trioxide
GB586874A (en) * 1944-06-21 1947-04-03 William Walker And Sons Ltd Improvements in the manufacture of heat-resistant and durable leathers and tanning agents therefor

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3081142A (en) * 1960-03-12 1963-03-12 Mezei Ernesto Vegetable one-bath pretanning process
US3927966A (en) * 1973-11-07 1975-12-23 Schill & Seilacher Process of producing a fatliquoring chrome tanning agent, composition containing same and method of using same

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