US2227863A - Extraction of tobacco with fluorochlorohydrocarbons - Google Patents

Extraction of tobacco with fluorochlorohydrocarbons Download PDF

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Publication number
US2227863A
US2227863A US190495A US19049538A US2227863A US 2227863 A US2227863 A US 2227863A US 190495 A US190495 A US 190495A US 19049538 A US19049538 A US 19049538A US 2227863 A US2227863 A US 2227863A
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Prior art keywords
tobacco
extraction
solvent
fluorochlorohydrocarbons
temperature
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Expired - Lifetime
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US190495A
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William W Rhodes
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KINETIC CHEMICALS Inc
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KINETIC CHEMICALS Inc
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Priority to US190495A priority Critical patent/US2227863A/en
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    • AHUMAN NECESSITIES
    • A24TOBACCO; CIGARS; CIGARETTES; SIMULATED SMOKING DEVICES; SMOKERS' REQUISITES
    • A24BMANUFACTURE OR PREPARATION OF TOBACCO FOR SMOKING OR CHEWING; TOBACCO; SNUFF
    • A24B15/00Chemical features or treatment of tobacco; Tobacco substitutes, e.g. in liquid form
    • A24B15/18Treatment of tobacco products or tobacco substitutes
    • A24B15/24Treatment of tobacco products or tobacco substitutes by extraction; Tobacco extracts
    • A24B15/26Use of organic solvents for extraction

Definitions

  • This invention relates to the treatment of The fluoro-chloro-methanes of the above list tobacco, more particularly it relates to the imrepresent the preferred compounds and of these provement of tobacco by solvent extraction of I prefer the monofluorochloromethanes. undesirable components.
  • the selective action of these compounds as to This invention has for an object the improvetarry matter is illustrated by the following table: 5 ment of tobacco by extraction of undesirable lmpurities.
  • a further object is the extraction of P fi P9 c at undesirable constituents from tobacco without a i? nic otin Ratio of impairing the desirable properties of the same.
  • the extraction can furthermore be performed at 20 such as aftFr grinding other Processmg 71th difierent stages of the preparation of the tobacco an aliphatic fiuorochlorohydrocarbon solvent. for use.
  • the followin example illustrates the The fiuumcmorohydmcarbc'ns used are extraction of tobacco which has been pretreated ably those which have relatively low boiling with ammonia;
  • Example III is not intended to be limited by thfi following one hundred pounds of uncured leaf tobacco x mp was moistened with dilute ammonia solution Example I (about 0.5% ammonia) and extracted in this One hundred pounds f l f t b w condition with 200# of CClzFz. This treatment tracted in a large vessel at a temperature of 20 o e about 30 of the tarry matter and Over. C. with monofluorotrichloromethane.
  • the temperature to be used may Vary over a the preceding examples with equally good wide range and depends upon not only the solsults- Among the useful compoundsare vent chosen but the pressure employed.
  • the extraction may be carried out between -40 CzHzClzFz, CzHClaFz CzHaClzF' and +100 Cpand preferably between -10 and cmzclr'a CzClaF'a CHzClF +50 C.
  • the particular temperature chosen de- CzHClzFa pends upon the particular solvent used and the which the extraction is carried out will depend entirely on the solvent and temperature at which the extraction is performed.
  • the pressure should at least be sumcient to keep the solvent in the liquid state.
  • CFzClz is used as the solvent at a temperature of 309 C.
  • the pressure will be about 98 pounds per square inch gauge, while it C2F4Cl2 is used at this temperature the pressure necessary will be only about 22 pounds per square inch gauge.
  • This invention presents the advantage that fire and health hazards which are encountered by the use of lower alkyl chlorides are eliminated.
  • a further advantage resides in the fact that the solvent may be quickly removed from the tobacco at low temperatures. thus obviating the higher temperatures necessarywith other solvents. Since overheating or tobacco is very deleterious, this'advantage is of considerable importance.
  • a still further advantage is the preferential solvent action exhibited by these solvents on theundesirable tarry matter found in tobacco.
  • Other advantages reside in the combination of non-inflammability, low boiling point, non-toxicity, non-corroslveness to equipment, and good solvent action on tars..

Description

Patented Jan. 7, 1941 EXTRACTION F TOBACCO WITH FLUORO- CHLOROHYDROCARBONS William w. Rhodes, Philadelphia, Pa, assignor. by mesne assignments, to Kinetic Chemicals, Inc., a corporation of Delaware No Drawing. Application February 14, 1938, Serial No. 190,495
4 Claims. (Cl. 131-443) This invention relates to the treatment of The fluoro-chloro-methanes of the above list tobacco, more particularly it relates to the imrepresent the preferred compounds and of these provement of tobacco by solvent extraction of I prefer the monofluorochloromethanes. undesirable components. The selective action of these compounds as to This invention has for an object the improvetarry matter is illustrated by the following table: 5 ment of tobacco by extraction of undesirable lmpurities. A further object is the extraction of P fi P9 c at undesirable constituents from tobacco without a i? nic otin Ratio of impairing the desirable properties of the same. Compound 'if gf removed, it; A still further object is to reduce the fire and A a B co 6 10 health hazards encountered in the solvent extraction of tobacco. Other objects will appear 4 9 0 3 16 hereinafter. 2'. 9 0: 1 29 The aboveand other objects are accomplished CH0] F by the following invention which comprises Mam ]ifiiiriIIIIIIIIIIIIIIIII 016 115 1.4 treating tobacco with a solvent which has a preferential action upon the tarry constituents. The extraction can be performed on dry or More particularly these objects are accomplished moist tobacco, it can be performed p P extracting tobacco in the form of leaves bacco which has been treated with other agents. In any Qther Physical state in which it m i t The extraction can furthermore be performed at 20 such as aftFr grinding other Processmg 71th difierent stages of the preparation of the tobacco an aliphatic fiuorochlorohydrocarbon solvent. for use. The followin example illustrates the The fiuumcmorohydmcarbc'ns used are extraction of tobacco which has been pretreated ably those which have relatively low boiling with ammonia;
points, for example, below 100 C.
The invention will be further understood but Example III is not intended to be limited by thfi following one hundred pounds of uncured leaf tobacco x mp was moistened with dilute ammonia solution Example I (about 0.5% ammonia) and extracted in this One hundred pounds f l f t b w condition with 200# of CClzFz. This treatment tracted in a large vessel at a temperature of 20 o e about 30 of the tarry matter and Over. C. with monofluorotrichloromethane. The s01- 55% 0f the mcotlne Originally in the tobaccovent was found to contain a high amount of The Separation of e o e t from e 6 tarry matter and a relatively small amount of trfwted material may be accompl y Simple nicotine. The resulting tobacco after complete dlstillation- The residual v n ay e removal of the solvent was good in appearance moved m the 00118-000 y passing Other and had xcellent, smuking properties inert gases over the treated tobacco or by a sim- Emmpze H ple warming of the treated mass to volatilize the solvent.
one hundred Pmmds of shredded tobacco was The quantity of solvent which will be used de- 40 countercurrently extracted at a temperature of pends largely upon the results desired If a 20 C. m0n0fl110r0d10h10r0methane under maxjIn-um removal of tar is desired be Pressure- The Savant was found upon Subse' preferable to use a larger quantity of solvent or quent treatment to wntain a large amount of to treat the same in a countercurrent system.
tarry matter and minor amounts of nicotine The results reported in the above table were ob- The tobacco was of good flavor Odo! and tained with a solvent tobacco ratio of 10 to l Peamnce and had smolfing characteristicsbut this ratio is merely illustrative of the process Other fluorochloro-aliphatic hydrocarbons can and t a limitation.
be substituted for the Specific ones described in The temperature to be used may Vary over a the preceding examples with equally good wide range and depends upon not only the solsults- Among the useful compoundsare vent chosen but the pressure employed. Thus CHClFz CzHClF C2H3C1Fz the extraction may be carried out between -40 CzHzClzFz, CzHClaFz CzHaClzF' and +100 Cpand preferably between -10 and cmzclr'a CzClaF'a CHzClF +50 C. The particular temperature chosen de- CzHClzFa pends upon the particular solvent used and the which the extraction is carried out will depend entirely on the solvent and temperature at which the extraction is performed. As a general rule the pressure should at least be sumcient to keep the solvent in the liquid state. For example, it CFzClz is used as the solvent at a temperature of 309 C., the pressure will be about 98 pounds per square inch gauge, while it C2F4Cl2 is used at this temperature the pressure necessary will be only about 22 pounds per square inch gauge.
This invention presents the advantage that fire and health hazards which are encountered by the use of lower alkyl chlorides are eliminated. A further advantage resides in the fact that the solvent may be quickly removed from the tobacco at low temperatures. thus obviating the higher temperatures necessarywith other solvents. Since overheating or tobacco is very deleterious, this'advantage is of considerable importance. A still further advantage is the preferential solvent action exhibited by these solvents on theundesirable tarry matter found in tobacco. Other advantages reside in the combination of non-inflammability, low boiling point, non-toxicity, non-corroslveness to equipment, and good solvent action on tars..
As many apparently widely different embodiments of this invention may be made without departing from the spirit and scope thereof, it is to be understood that we do not limit ourselves to the specific embodiments thereof except as defined by the appended claims. f
I claim:
1. The process which consists of subjecting tobacco to a liquid phase extraction with a lowboiling halogenated solvent taken from the class consisting of the normally gaseous fluorochloromethanes.
2. The process which consists of subjecting tobacco to a liquid phase extraction with dichlorodlfluoromethane.
3. The process which consists of subjecting tobacco to a liquid phase extraction with dichloromonofluoromethane.
4. The process which consists of subjecting tobacco to a liquid phase extraction with trichloromonofluoromethane. I
WILLIAM W. RHODES.
US190495A 1938-02-14 1938-02-14 Extraction of tobacco with fluorochlorohydrocarbons Expired - Lifetime US2227863A (en)

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Cited By (17)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE1082541B (en) * 1957-04-12 1960-05-25 Sasmoco Sa Process for the continuous treatment of tobacco
US3096773A (en) * 1957-04-12 1963-07-09 Sasmoco Sa Process for treating tobacco and tobacco obtained by said process
DE1170848B (en) * 1958-04-11 1964-05-21 Sasmoco Sa Process for treating tobacco with metal compounds
US3394709A (en) * 1964-04-13 1968-07-30 Inca Inks Treatment of tobacco
US3575178A (en) * 1969-03-13 1971-04-20 Reynolds Tobacco Co R A process for increasing the filling capacity of tobacco
USRE30693E (en) * 1975-03-17 1981-08-04 Reynolds Leasing Corporation Process for increasing the filling capacity of tobacco
US4628947A (en) * 1985-07-05 1986-12-16 Philip Morris Incorporated Process for modifying the flavor characteristics of bright tobacco
EP0280817A2 (en) * 1986-12-29 1988-09-07 Philip Morris Products Inc. Process for the removal of basic materials from plant products
US4967771A (en) * 1988-12-07 1990-11-06 R. J. Reynolds Tobacco Company Process for extracting tobacco
US5018540A (en) * 1986-12-29 1991-05-28 Philip Morris Incorporated Process for removal of basic materials
US5025812A (en) * 1989-08-10 1991-06-25 R. J. Reynolds Tobacco Company Tobacco processing
US5065775A (en) * 1990-02-23 1991-11-19 R. J. Reynolds Tobacco Company Tobacco processing
US5131414A (en) * 1990-02-23 1992-07-21 R. J. Reynolds Tobacco Company Tobacco processing
US5234008A (en) * 1990-02-23 1993-08-10 R. J. Reynolds Tobacco Company Tobacco processing
US20040112394A1 (en) * 2002-07-18 2004-06-17 Val Krukonis Reduction of constituents in tobacco
US20070137666A1 (en) * 2005-12-13 2007-06-21 Philip Morris Usa Inc. Incorporation of ammonia-release compounds in smoking articles
US8887737B2 (en) 2005-07-29 2014-11-18 Philip Morris Usa Inc. Extraction and storage of tobacco constituents

Cited By (26)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE1082541B (en) * 1957-04-12 1960-05-25 Sasmoco Sa Process for the continuous treatment of tobacco
US3096773A (en) * 1957-04-12 1963-07-09 Sasmoco Sa Process for treating tobacco and tobacco obtained by said process
DE1170848B (en) * 1958-04-11 1964-05-21 Sasmoco Sa Process for treating tobacco with metal compounds
US3394709A (en) * 1964-04-13 1968-07-30 Inca Inks Treatment of tobacco
US3575178A (en) * 1969-03-13 1971-04-20 Reynolds Tobacco Co R A process for increasing the filling capacity of tobacco
USRE30693E (en) * 1975-03-17 1981-08-04 Reynolds Leasing Corporation Process for increasing the filling capacity of tobacco
US4628947A (en) * 1985-07-05 1986-12-16 Philip Morris Incorporated Process for modifying the flavor characteristics of bright tobacco
EP0207809A2 (en) 1985-07-05 1987-01-07 Philip Morris Products Inc. Process for modifying the flavour characterstics of bright tobacco
EP0280817A2 (en) * 1986-12-29 1988-09-07 Philip Morris Products Inc. Process for the removal of basic materials from plant products
EP0280817A3 (en) * 1986-12-29 1990-05-16 Philip Morris Products Inc. Process for the removal of basic materials from plant products
US5018540A (en) * 1986-12-29 1991-05-28 Philip Morris Incorporated Process for removal of basic materials
US4967771A (en) * 1988-12-07 1990-11-06 R. J. Reynolds Tobacco Company Process for extracting tobacco
US5025812A (en) * 1989-08-10 1991-06-25 R. J. Reynolds Tobacco Company Tobacco processing
US5065775A (en) * 1990-02-23 1991-11-19 R. J. Reynolds Tobacco Company Tobacco processing
US5131414A (en) * 1990-02-23 1992-07-21 R. J. Reynolds Tobacco Company Tobacco processing
US5234008A (en) * 1990-02-23 1993-08-10 R. J. Reynolds Tobacco Company Tobacco processing
US20110067715A1 (en) * 2002-07-18 2011-03-24 Us Smokeless Tobacco Co. Reduction of constituents in tobacco
US7798151B2 (en) 2002-07-18 2010-09-21 Us Smokeless Tobacco Co. Reduction of constituents in tobacco
US20040112394A1 (en) * 2002-07-18 2004-06-17 Val Krukonis Reduction of constituents in tobacco
US8555895B2 (en) 2002-07-18 2013-10-15 U.S. Smokeless Tobacco Company Llc Reduction of constituents in tobacco
US10045557B2 (en) 2002-07-18 2018-08-14 Us Smokeless Tobacco Co. Reduction of constituents in tobacco
US8887737B2 (en) 2005-07-29 2014-11-18 Philip Morris Usa Inc. Extraction and storage of tobacco constituents
US20070137666A1 (en) * 2005-12-13 2007-06-21 Philip Morris Usa Inc. Incorporation of ammonia-release compounds in smoking articles
US8042552B2 (en) 2005-12-13 2011-10-25 Philip Morris Usa Inc. Incorporation of ammonia-release compounds in smoking articles
US8555897B2 (en) 2005-12-13 2013-10-15 Philip Morris Usa Inc. Method of making a cigarette and method of reducing cytotoxicity in tobacco smoke
US10051883B2 (en) 2005-12-13 2018-08-21 Philip Morris Usa Inc. Incorporation of ammonia release compounds in smoking articles

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