US1066877A - Art of purifying chloroform. - Google Patents

Art of purifying chloroform. Download PDF

Info

Publication number
US1066877A
US1066877A US72937312A US1912729373A US1066877A US 1066877 A US1066877 A US 1066877A US 72937312 A US72937312 A US 72937312A US 1912729373 A US1912729373 A US 1912729373A US 1066877 A US1066877 A US 1066877A
Authority
US
United States
Prior art keywords
chloroform
chlorin
fluid
purifying
free
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
Application number
US72937312A
Inventor
Victor C Best
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Individual
Original Assignee
Individual
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Individual filed Critical Individual
Priority to US72937312A priority Critical patent/US1066877A/en
Application granted granted Critical
Publication of US1066877A publication Critical patent/US1066877A/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Images

Classifications

    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C17/00—Preparation of halogenated hydrocarbons
    • C07C17/38—Separation; Purification; Stabilisation; Use of additives

Definitions

  • Uhloroform as commonly produced by the methods heretofore practised, contains a certain percentage of free chlorin and volatile oils, the resence of which is objectionable, especially when the chloroform is inhaled, as for anesthetizing purposes, as they are injurious to the human body, often producing deadly effects, the free volatile oils in the chloroform acting on the respiratory and cardiac centers in the bod and causing a disorganization of the physiological functions. It has been found that by removing the free chlorin and the volatile oils, the chloroform, thus purified, is purged of its deadly effects without afi'ectingit as an anesthetizing medium.
  • My object is to provide a process whereby the free chlorin .and volatile oils may be effectually removed from chloroform with the above-stated advantageous results, my
  • the apparatus illustrated comprises a flask 1, a receptacle 2 located in the flask and spaced from the wall thereof; said receptacle being secured at its open upper end in the mouth 3 of the flask and opening into one end of a vapor-conducting tube l secured to the upper end of the flask, and which tube, in practice, would open at its opposite end into a condensing-chamber (not shown), and a steam-coil 5 surrounding the receptacle 2 in the space between the latter and said flask, and extendin at its opposite ends 6 and 7 through said flask for connection with a suitable source of respectively.
  • the chloroform to be purified is poured into the receptacle 2 to partially till the latter, as, for example, up to the level indicated by the line a: and a fluid of the character above stated and indicated at 8, then poured into'the receptacle 2 onto the top of the chloroform, the said fluid floating on the latter and extending, as for example, to a level indicated by the line "y.
  • any fluid capable of chemically combining with the free chlorin in the chloroform vapor may be used, it being preferred, however, that the fluid be a hyper-saturated solution of a base, alkali, salt, or any other substance capable of chemically combining with the free chlorin in the chloroform vapor, and that where an alkali is used, it be potassium-hydroxid (KOH), and that where a salt is used, it be silver-nitrate (AGNO).
  • KOH potassium-hydroxid
  • AGNO silver-nitrate
  • the chloroform is then heated to vaporize it, as by passing steam through the coil 5, to heat the chloroform to as high a degree as possible, but sufliciently low to prevent the vaporizing of said solution and the forcing from the latter of the base, alkali, salt or other substance therein of the character above stated, as the case may be, by the action of the vaporized chloroform which passes in the form of vapor through the solution, the heating of the chloroform to about 200 F.
  • the free chlorin in the chloroform combineswith the base, alkali, salt or other substance therein of the character above stated, as the case may be, and the volatile oils in the chloroform are held back and condensed by said fluid, with the result of removing the free chlorin and volatile oils from the chloroform vapor, which latter passes from the receptacle 2 and tube 4 in the desired purified condition into the condenser.
  • fluid may be used within my inventionwhich is initially combined with chlorin, provided it does not contain such an amount of chlorin that it will not take up free chlorin in the chloroform when the latter in vaporized condition is passed through said fluid.

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Heterocyclic Carbon Compounds Containing A Hetero Ring Having Oxygen Or Sulfur (AREA)

Description

V. 0. BEST. ART OF PURIFYING GHLOROFORM.
APPLICATION FILED NOV. 4, 1912.
Patented July 8, 1913.
vro'ron 0. BEST, or OAK PARK, lL mors.
an or PURIFYING cnnonorongm.
Bpecification of Letters latent.
Patented July 8, 1913.
Application filed November 4, 1912. Serial No. 729,373.
To all whom it may concern:
Be it known that I, VICTOR C. Beer, a subject of the King of Great Britain, residing at Oak Park, in the county of Cook and State of Illinois, have invented a new and useful Improvement in the Art of Purifying Chloroform, of which the following is a specification.
Uhloroform, as commonly produced by the methods heretofore practised, contains a certain percentage of free chlorin and volatile oils, the resence of which is objectionable, especially when the chloroform is inhaled, as for anesthetizing purposes, as they are injurious to the human body, often producing deadly effects, the free volatile oils in the chloroform acting on the respiratory and cardiac centers in the bod and causing a disorganization of the physiological functions. It has been found that by removing the free chlorin and the volatile oils, the chloroform, thus purified, is purged of its deadly effects without afi'ectingit as an anesthetizing medium.
My object is to provide a process whereby the free chlorin .and volatile oils may be effectually removed from chloroform with the above-stated advantageous results, my
improved process, generally stated, consisting in passing the chloroform in vaporized condition through a fluid capable of chemically combining with free chlorin in the chloroform vapor.
In practising my new process I may use any desirable apparatus, the accompanying drawing illustrating, by a view in sectional elevation, a form of apparatus which may be used to advantage.
The apparatus illustrated comprises a flask 1, a receptacle 2 located in the flask and spaced from the wall thereof; said receptacle being secured at its open upper end in the mouth 3 of the flask and opening into one end of a vapor-conducting tube l secured to the upper end of the flask, and which tube, in practice, would open at its opposite end into a condensing-chamber (not shown), and a steam-coil 5 surrounding the receptacle 2 in the space between the latter and said flask, and extendin at its opposite ends 6 and 7 through said flask for connection with a suitable source of respectively.
The chloroform to be purified is poured into the receptacle 2 to partially till the latter, as, for example, up to the level indicated by the line a: and a fluid of the character above stated and indicated at 8, then poured into'the receptacle 2 onto the top of the chloroform, the said fluid floating on the latter and extending, as for example, to a level indicated by the line "y. Any fluid capable of chemically combining with the free chlorin in the chloroform vapor may be used, it being preferred, however, that the fluid be a hyper-saturated solution of a base, alkali, salt, or any other substance capable of chemically combining with the free chlorin in the chloroform vapor, and that where an alkali is used, it be potassium-hydroxid (KOH), and that where a salt is used, it be silver-nitrate (AGNO The chloroform is then heated to vaporize it, as by passing steam through the coil 5, to heat the chloroform to as high a degree as possible, but sufliciently low to prevent the vaporizing of said solution and the forcing from the latter of the base, alkali, salt or other substance therein of the character above stated, as the case may be, by the action of the vaporized chloroform which passes in the form of vapor through the solution, the heating of the chloroform to about 200 F. producing satisfactory results. By passing the chloroform, in vaporized condition, through the fluid 8, the free chlorin in the chloroform combineswith the base, alkali, salt or other substance therein of the character above stated, as the case may be, and the volatile oils in the chloroform are held back and condensed by said fluid, with the result of removing the free chlorin and volatile oils from the chloroform vapor, which latter passes from the receptacle 2 and tube 4 in the desired purified condition into the condenser. The passing of the chloroform in vaporized condition through the fluid, as above set forth, is of great advantage, as the great molecular expansion of the chloroform, when heated, causes the molecules thereof to be spread apart, thus enhancing the subjection of the chloroform molecules to the fluid 8 and effectually free will free chlorin in the chloroform vapor is much greater than if the fluid used, be initiall combined with chlorin. However, it be readily understood that, if desired, a
fluid may be used within my inventionwhich is initially combined with chlorin, provided it does not contain such an amount of chlorin that it will not take up free chlorin in the chloroform when the latter in vaporized condition is passed through said fluid.
What I claim as new and desire to secure by Letters Patent is 1. The process of purifying chloroform, which consists in passing the chloroform in vaporized condition through a fluid capable of chemically combining with free chlorin in the chloroform vapor.
2. The process of purifying chloroform, which consists in passing the chloroform in vaporized condition through a solution of a substance capable of chemically combining with free chlorin in the chloroform vapor.
3. The process of purifying chloroform,-
which consists in passing the chloroform in vaporized condition through a solution of an inorganic substance capable of chemivaporized condition through a fluid uncombined with chlorin, but capable of chemi-' cally combining with free chlorin in the chloroform vapor. e
5. The process of purifying chloroform which consists in passing the chloroform in vaporized condition through a solution of a salt capable of combining with chlorin.
6. The process of purifying chloroform, which consists in passing the chloroform in vaporized condition through a solution of a salt uncombined with chlorin, but capable of combining with chlorin.
7. The process of purifying chloroform, which consists in passing the chloroform in vaporized condition through a solution of NELLIE B. DEARBORN; QTTILIE C. AvIsUs.
US72937312A 1912-11-04 1912-11-04 Art of purifying chloroform. Expired - Lifetime US1066877A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
US72937312A US1066877A (en) 1912-11-04 1912-11-04 Art of purifying chloroform.

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US72937312A US1066877A (en) 1912-11-04 1912-11-04 Art of purifying chloroform.

Publications (1)

Publication Number Publication Date
US1066877A true US1066877A (en) 1913-07-08

Family

ID=3135120

Family Applications (1)

Application Number Title Priority Date Filing Date
US72937312A Expired - Lifetime US1066877A (en) 1912-11-04 1912-11-04 Art of purifying chloroform.

Country Status (1)

Country Link
US (1) US1066877A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3107205A (en) * 1960-09-16 1963-10-15 John J Moran Laboratory distillation apparatus
US4650916A (en) * 1983-03-07 1987-03-17 Ppg Industries, Inc. Removal of molecular chlorine from 1,2-dichloroethane compositions contaminated with molecular chlorine

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3107205A (en) * 1960-09-16 1963-10-15 John J Moran Laboratory distillation apparatus
US4650916A (en) * 1983-03-07 1987-03-17 Ppg Industries, Inc. Removal of molecular chlorine from 1,2-dichloroethane compositions contaminated with molecular chlorine

Similar Documents

Publication Publication Date Title
US511288A (en) Apparatus for producing a liquid product of smoke
US2570041A (en) Soldering iron stand
GB992697A (en) Improvements in or relating to processes and apparatus for deodorising oils and fats
US1925559A (en) Vacuum extraction of cod liver oil
US902535A (en) Method of condensing volatile metals.
US1506444A (en) Process of refining oil
DE215005C (en)
US1162036A (en) Process of redistillation of products resulting from destructive distillation of resinous wood.
DE345960C (en) Device for degassing and evaporating liquids
GB217945A (en) Improvements in or relating to evaporator apparatus
US56852A (en) Improvement in apparatus for distilling petroleum
DE958238C (en) Method and device for generating high negative pressures by means of single or multi-stage diffusion pumps
US1580956A (en) Process for dehydrating emulsions
US492419A (en) Still-lining
US550716A (en) Herman frasch
US774171A (en) Process of distilling liquids.
AT70266B (en) Process for evaporating milk and other easily decomposable liquids.
AT68081B (en) Method and device for generating cold.
DE579022C (en) Device for the distillation of high-boiling substances
DE739863C (en) Process and device for evaporation of liquids
US1062750A (en) Inhaling apparatus.
AT31756B (en) Process for the distillation of glycerine.
US591683A (en) Disinfecting compound and apparatus foe
DE494502C (en) Process and device for the evaporation of caustic or crust-forming solutions
DE697693C (en) Cooling container for bare goods to be cooled