US1917073A - Method of stabilizing chlorinated aliphatic hydrocarbons - Google Patents
Method of stabilizing chlorinated aliphatic hydrocarbons Download PDFInfo
- Publication number
- US1917073A US1917073A US618693A US61869332A US1917073A US 1917073 A US1917073 A US 1917073A US 618693 A US618693 A US 618693A US 61869332 A US61869332 A US 61869332A US 1917073 A US1917073 A US 1917073A
- Authority
- US
- United States
- Prior art keywords
- chlorinated aliphatic
- hydrocarbon
- chlorinated
- aliphatic hydrocarbons
- mercaptan
- 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
- 150000001338 aliphatic hydrocarbons Chemical class 0.000 title description 10
- 238000000034 method Methods 0.000 title description 4
- 230000000087 stabilizing effect Effects 0.000 title 1
- 239000000203 mixture Substances 0.000 description 16
- 229930195733 hydrocarbon Natural products 0.000 description 15
- 150000002430 hydrocarbons Chemical class 0.000 description 15
- VZGDMQKNWNREIO-UHFFFAOYSA-N tetrachloromethane Chemical compound ClC(Cl)(Cl)Cl VZGDMQKNWNREIO-UHFFFAOYSA-N 0.000 description 14
- 238000000354 decomposition reaction Methods 0.000 description 12
- LSDPWZHWYPCBBB-UHFFFAOYSA-N Methanethiol Chemical compound SC LSDPWZHWYPCBBB-UHFFFAOYSA-N 0.000 description 11
- 239000004215 Carbon black (E152) Substances 0.000 description 9
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 8
- 229950005499 carbon tetrachloride Drugs 0.000 description 7
- 150000008280 chlorinated hydrocarbons Chemical class 0.000 description 7
- 238000004821 distillation Methods 0.000 description 7
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 6
- 229910052802 copper Inorganic materials 0.000 description 6
- 239000010949 copper Substances 0.000 description 6
- 239000003112 inhibitor Substances 0.000 description 6
- 238000010992 reflux Methods 0.000 description 5
- HUMNYLRZRPPJDN-UHFFFAOYSA-N benzaldehyde Chemical compound O=CC1=CC=CC=C1 HUMNYLRZRPPJDN-UHFFFAOYSA-N 0.000 description 4
- WQAQPCDUOCURKW-UHFFFAOYSA-N butanethiol Chemical compound CCCCS WQAQPCDUOCURKW-UHFFFAOYSA-N 0.000 description 4
- 230000002401 inhibitory effect Effects 0.000 description 4
- 229910052742 iron Inorganic materials 0.000 description 4
- 239000002184 metal Substances 0.000 description 4
- 229910052751 metal Inorganic materials 0.000 description 4
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 4
- KNKRKFALVUDBJE-UHFFFAOYSA-N 1,2-dichloropropane Chemical compound CC(Cl)CCl KNKRKFALVUDBJE-UHFFFAOYSA-N 0.000 description 3
- CYTYCFOTNPOANT-UHFFFAOYSA-N Perchloroethylene Chemical group ClC(Cl)=C(Cl)Cl CYTYCFOTNPOANT-UHFFFAOYSA-N 0.000 description 3
- YXFVVABEGXRONW-UHFFFAOYSA-N Toluene Chemical compound CC1=CC=CC=C1 YXFVVABEGXRONW-UHFFFAOYSA-N 0.000 description 3
- 125000004108 n-butyl group Chemical group [H]C([H])([H])C([H])([H])C([H])([H])C([H])([H])* 0.000 description 3
- 238000011084 recovery Methods 0.000 description 3
- 239000002904 solvent Substances 0.000 description 3
- 229950011008 tetrachloroethylene Drugs 0.000 description 3
- 229910000831 Steel Inorganic materials 0.000 description 2
- XSTXAVWGXDQKEL-UHFFFAOYSA-N Trichloroethylene Chemical group ClC=C(Cl)Cl XSTXAVWGXDQKEL-UHFFFAOYSA-N 0.000 description 2
- 230000009471 action Effects 0.000 description 2
- 125000001931 aliphatic group Chemical group 0.000 description 2
- 238000009835 boiling Methods 0.000 description 2
- 125000001309 chloro group Chemical group Cl* 0.000 description 2
- 238000005108 dry cleaning Methods 0.000 description 2
- 239000000975 dye Substances 0.000 description 2
- 239000004615 ingredient Substances 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- QNGNSVIICDLXHT-UHFFFAOYSA-N para-ethylbenzaldehyde Natural products CCC1=CC=C(C=O)C=C1 QNGNSVIICDLXHT-UHFFFAOYSA-N 0.000 description 2
- 239000010959 steel Substances 0.000 description 2
- UBOXGVDOUJQMTN-UHFFFAOYSA-N trichloroethylene Natural products ClCC(Cl)Cl UBOXGVDOUJQMTN-UHFFFAOYSA-N 0.000 description 2
- LDVVMCZRFWMZSG-OLQVQODUSA-N (3ar,7as)-2-(trichloromethylsulfanyl)-3a,4,7,7a-tetrahydroisoindole-1,3-dione Chemical compound C1C=CC[C@H]2C(=O)N(SC(Cl)(Cl)Cl)C(=O)[C@H]21 LDVVMCZRFWMZSG-OLQVQODUSA-N 0.000 description 1
- MKXQDWBMYIZXQL-UHFFFAOYSA-N 1,2,2,3,3,5-hexachloropentane Chemical compound ClCCC(Cl)(Cl)C(Cl)(Cl)CCl MKXQDWBMYIZXQL-UHFFFAOYSA-N 0.000 description 1
- 239000005745 Captan Substances 0.000 description 1
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 1
- XDTMQSROBMDMFD-UHFFFAOYSA-N Cyclohexane Chemical compound C1CCCCC1 XDTMQSROBMDMFD-UHFFFAOYSA-N 0.000 description 1
- RWSOTUBLDIXVET-UHFFFAOYSA-N Dihydrogen sulfide Chemical class S RWSOTUBLDIXVET-UHFFFAOYSA-N 0.000 description 1
- 206010013710 Drug interaction Diseases 0.000 description 1
- 229910000792 Monel Inorganic materials 0.000 description 1
- 230000008901 benefit Effects 0.000 description 1
- 229940117949 captan Drugs 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 150000001768 cations Chemical class 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 239000002361 compost Substances 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 238000005260 corrosion Methods 0.000 description 1
- 230000007797 corrosion Effects 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 238000010348 incorporation Methods 0.000 description 1
- 230000003993 interaction Effects 0.000 description 1
- 150000002739 metals Chemical class 0.000 description 1
- 239000003208 petroleum Substances 0.000 description 1
- 230000009467 reduction Effects 0.000 description 1
- 230000000717 retained effect Effects 0.000 description 1
- 150000003839 salts Chemical class 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 239000012808 vapor phase Substances 0.000 description 1
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
- C07C17/42—Use of additives, e.g. for stabilisation
Definitions
- the invention relates to methods of inhibiting the decomposition of chlorinated al1- phatic hydrocarbons and to the improved product thereby obtained.
- chlorinated aliphatic hydrocarbons e. g. carbon tetrachlo ride, tetrachloroethylene, propylene chloride, etc.
- decomposition during storage and/or distillation, particularly in the presenceof moisture
- chlorinated hydrocarbons e. g. carbon tetrachlo ride, tetrachloroethylene, propylene chloride, etc.
- this tendency toward decomposition is more chlorinated hydrocarbons corrosive 'proppronounced when such hydrocarbons are in contact with copper, as during distillation in dry cleaning solvent recovery, etc.
- chlorinated allphatic hydrocarbons having incorporated therewith compounds such as benzaldehyde, cyclohexane, various dyes, petroleum oil fractions,
- chlorinated aliphatic hydrocarbons can be rendered stable I during storage and distillation, particularly several approved combinations of ingredients embodylng our invention, such disclosed [means constituting, however, but several of various forms in which the principle of the invention may be used.
- the proportions of the mercaptan which we have found suflicient in admixture with chlorinated aliphatic hydrocarbons to suppress decomposition, is exceedingly small, e. g. between about 0.001 and 0.1 per cent by volume.
- the selection of the mercaptan in any particular instance will be determined somewhat by the boiling point of the hydro--' carbon, since it is'desirable that the boiling point of the mercaptan and that of the hydrocarbon'be reasonably close together in order that the mercaptan will be retained therein during distillation.
- Table I shows the results which have been obtained in practicing our invention, using various mercaptans for inhibiting the decompositions of carbontetrachloride.
- recovery of the solvent composition is accomplishedby distillation; and, vapor phase degreasin of metallic articles.
- A- compositionof matter comprising a i chlorinated aliphatic h drocarbon and a relatively small amount 0 a mercaptan.
- a composition of matter oomprisin a chlorinated aliphatic hydrocarbon and 3.
- a composition of matter comprising a chlorinated aliphatic hydrocarbon and about 0-0051) cent by volume of n-butyl mer-.v aPtan.
- composition of -matter comprising 118mg percent relatively small 0.1 per cent by volume I I 6.
- a composition-I of matter comprising tetrachloroethylene and a relatively amount ofamercaptan. -7. 'A- composition of matter comprising.
- tetrachloroethylene and about 0.005 per cent by volume of n-butyl mercaptan. 8.
- a composition. of matter comprising trichloroethylene and a relatively. small amount of a mercaptan.
- a composition of matter comp triehloroethylene and about 0.005 per cent by J volume-of n-butyl mercaptan.
- a composition of matter comprisin a chlorinated aliphatic hydrocarbon which as at least two chlorine atoms in the molecule and a relatively small amount of a mercaptan. .14.
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Description
Patented July 4, 1933 j UNITED STATES PATENT-. oFFis LEROY O. STEWART AND LEE DE FREE, OF MIDLAND, MICHIGAN, ASSIGNORS'TO' TEE DOW CHEMICAL COMPANY, OF MIDLAND, MICHIGAN, A CORPORATION OF MICHIGAN METHOD OF STABITIIZING CHLORINATED ALIPEATIG HYDBOGARBONS No Drawing.
The invention relates to methods of inhibiting the decomposition of chlorinated al1- phatic hydrocarbons and to the improved product thereby obtained.
. The marked tendency. of chlorinated aliphatic hydrocarbons, e. g. carbon tetrachlo ride, tetrachloroethylene, propylene chloride, etc. toward decomposition during storage and/or distillation, particularly in the presenceof moisture, is well known. In general this tendency toward decomposition is more chlorinated hydrocarbons corrosive 'proppronounced when such hydrocarbons are in contact with copper, as during distillation in dry cleaning solvent recovery, etc. Furthermore, in connection with the distillation of the aforementioned chlorinated hydrocarbons in copper recovery stills, it has been shown that by inter-action between the decomposition products of the hydrocarbons and the metal of the still,'co pper salts are formed which markedly accelerate the decompositlon of the hydrocarbon. Thus the rate at which the solvent breaks down increases progressively when in contact with copper. Such decomposition quite generally imparts to the erties which render them objectionable for many purposes.
To overcome this difficulty it has been pro' posed to add to the chlorinated hydrocarbons certain materials which are capable of 1nh1b1ting the tendency thereof toward-decomposr tion. For example, chlorinated allphatic hydrocarbons having incorporated therewith compounds such as benzaldehyde, cyclohexane, various dyes, petroleum oil fractions,
toluene, etc: have been proposed as compost tions of matter wherein the tendency o f chlorinated hydrocarbon toward decomposltlon 1 s suppressed. However, the use as decom cs1- tion inhibitors of-compounds such as the oregoing has been disadvantageous, prlncipally because of the relatively large proportion of the inhibitor that must be included with the chlorinated hydrocarbon to render it efliectlve. Other disadvantages, suchas coloration of the mixture of inhibitor and hydrocarbon, as I in the case of dyes; separation of the inhibitor and hydrocarbon during distillation, as in the case of benzaldehyde, etc.; have attached to 1932. Serial No. 618,693.
the use of the type of inhibitors, hereinbefore recited.
We have now found that chlorinated aliphatic hydrocarbons can be rendered stable I during storage and distillation, particularly several approved combinations of ingredients embodylng our invention, such disclosed [means constituting, however, but several of various forms in which the principle of the invention may be used.
The proportions of the mercaptan, which we have found suflicient in admixture with chlorinated aliphatic hydrocarbons to suppress decomposition, is exceedingly small, e. g. between about 0.001 and 0.1 per cent by volume. The selection of the mercaptan in any particular instance will be determined somewhat by the boiling point of the hydro--' carbon, since it is'desirable that the boiling point of the mercaptan and that of the hydrocarbon'be reasonably close together in order that the mercaptan will be retained therein during distillation.
.The following Table I shows the results which have been obtained in practicing our invention, using various mercaptans for inhibiting the decompositions of carbontetrachloride. As a measure of the decomposition occurring in the chlorinated hydrocarbon during contact with copper and iron, we have determined the milligrams of metal corroded away-per square decimeter of area exposed to the action of the hydrocarbon at refluxing temperature'for 46 hours in the presence of water. The tests were conducted by partially immersing a weighed and measured strip of metal in a measured volume of the chlorinated hydrocarbon containing the in,- hibitor in a round-bottomed flask, adding me II Milligrams loss per square decimeter v Hydrocarbon p r No in Mereaphlbltm' tan Carbon tetrachloride 14,800 22" Tetrachloroethylene.- 412 7 orolorm 231 y 70 Trichloroethylenb---- 1 92 25 Propylene chloride 43 l1 as I 507 Carbon tetrachloride 286 Tettachloroethylene-.-
,Car ntetrachlorid 25 50%Trichloroethylene 90% arbon tetrachlorid 23 107 Propylene chloride Mil-Te hl'oroethy lene my 17 10% Propylene-chloride about 40 percent by volume of water to the mixture in the flask, connecting the flask to a refluxing column; and heating the contents of the flask at refluxing temperature. The
amount of inhibitor employed is shown in per cent by volume of the carbon tetrachloride.
.The 'decomposition-inhibiting effect of incorporating approximately 0.005 per cent by volume of n-butyl mer'captan with various chlorinated aliphatic hydrocarbons and mixtures thereof is shown in the following Table II, which also gives as the measure of the decomposition. occurring in the'particular hydrocarbon or mixture the milligrams of copper corroded away per square decimeter of area exposed to the action of the hydrocarbon at refluxing temperature for 46 hours in the presence of water. r
From the foregoing tables it is readily to be seen that the incorporation of a'relatively small amount of La 'mercaptan with chlori-- nated aliphatic hydrocarbons results in a'distinct reduction of the decomposition occurrin in the hydrocarbon when in'c'ontact wit copper or iron even under the extremely severe conditions of continuous refluxing over a 46 hour period of time in the presence 1 of water. Further, we have determined that a similar benefit inures to the aforementioned hydrocarbons from the admixture therewith of-a me'rcaptan when incontact with other metals, e. g. iron,- steel, .tin, .Monel metal,
. composition.
vtween about 0.001 and of a mercaptan.
carbontetrachloride and a such hydrocarbons upon exposure to sunlight is also generally'inhibited in our new be noted is the effect upon Particularly to the decomposltion rate caused by incorporating a mercaptan with carbon tetrachloride, or mixtures thereof with various other chlorinated aliphatic hydrocarbons. The tables show that the addition of only 0.005 per cent of n-butyl mercaptanreduces the amount of corrosion, or, suppresses the decomposition,
substantially inhibited, and such mixtures may safely be stored or shipped in iron or steel containers.
' Among the especially advantageous appli cations which can be made of our improved composition of matter are (1) dry cleaning,
wherein recovery of the solvent composition is accomplishedby distillation; and, vapor phase degreasin of metallic articles.
Other modes of app yifig the principle of our invention maybe employed instead of the one explained, change bemg' made as regards the materials employed, provided the ing're dients stated by any of the following I or the equivalent of such stated ingredients be employed.
We therefore particularly point out and distinctly-claim as our invention claims 1. A- compositionof matter comprising a i chlorinated aliphatic h drocarbon and a relatively small amount 0 a mercaptan.
2. A composition of matter oomprisin a chlorinated aliphatic hydrocarbon and 3. A composition of matter comprising a chlorinated aliphatic hydrocarbon and about 0-0051) cent by volume of n-butyl mer-.v aPtan.
4. A composition of -matter comprising 118mg percent relatively small 0.1 per cent by volume I I 6. A composition-I of matter comprising tetrachloroethylene and a relatively amount ofamercaptan. -7. 'A- composition of matter comprising.
tetrachloroethylene and about 0.005 per cent by volume of n-butyl mercaptan. 8. A composition. of matter comprising trichloroethylene and a relatively. small amount of a mercaptan.
.9. A composition of matter comp triehloroethylene and about 0.005 per cent by J volume-of n-butyl mercaptan.
13. A composition of matter comprisin a chlorinated aliphatic hydrocarbon which as at least two chlorine atoms in the molecule and a relatively small amount of a mercaptan. .14. The method of inhibiting the decomsition of chlorinated aliphatic hydrocarins having, at least two chlorine atoms in the molecule which consists in incorporating therewith a relatively small amount of a mercaptan.
Signed by us this 17th day of June, 1932.
L'EROY C. STEWART. LEE DE FREE.
Priority Applications (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US618693A US1917073A (en) | 1932-06-22 | 1932-06-22 | Method of stabilizing chlorinated aliphatic hydrocarbons |
| GB14556/33A GB401210A (en) | 1932-06-22 | 1933-05-19 | Improvement in method of stabilising chlorinated aliphatic hydrocarbons |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US618693A US1917073A (en) | 1932-06-22 | 1932-06-22 | Method of stabilizing chlorinated aliphatic hydrocarbons |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US1917073A true US1917073A (en) | 1933-07-04 |
Family
ID=24478757
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US618693A Expired - Lifetime US1917073A (en) | 1932-06-22 | 1932-06-22 | Method of stabilizing chlorinated aliphatic hydrocarbons |
Country Status (2)
| Country | Link |
|---|---|
| US (1) | US1917073A (en) |
| GB (1) | GB401210A (en) |
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2422484A (en) * | 1943-10-30 | 1947-06-17 | Standard Oil Dev Co | Stabilized xylidine |
| US2510849A (en) * | 1946-04-26 | 1950-06-06 | Standard Oil Dev Co | Method of stabilizing aromatic amines |
| US2621215A (en) * | 1950-05-18 | 1952-12-09 | Diamond Alkali Co | Tetrachloroethylene stabilized by 2-halothiophene |
| US2704756A (en) * | 1952-05-14 | 1955-03-22 | Argus Chemical Lab Inc | Organic derivatives of tetravalent tin and compositions containing the same |
| US2998462A (en) * | 1959-11-13 | 1961-08-29 | Dow Chemical Co | Stable solvent compositions |
| US2999886A (en) * | 1959-11-13 | 1961-09-12 | Dow Chemical Co | Stable solvent compositions |
-
1932
- 1932-06-22 US US618693A patent/US1917073A/en not_active Expired - Lifetime
-
1933
- 1933-05-19 GB GB14556/33A patent/GB401210A/en not_active Expired
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2422484A (en) * | 1943-10-30 | 1947-06-17 | Standard Oil Dev Co | Stabilized xylidine |
| US2510849A (en) * | 1946-04-26 | 1950-06-06 | Standard Oil Dev Co | Method of stabilizing aromatic amines |
| US2621215A (en) * | 1950-05-18 | 1952-12-09 | Diamond Alkali Co | Tetrachloroethylene stabilized by 2-halothiophene |
| US2704756A (en) * | 1952-05-14 | 1955-03-22 | Argus Chemical Lab Inc | Organic derivatives of tetravalent tin and compositions containing the same |
| US2998462A (en) * | 1959-11-13 | 1961-08-29 | Dow Chemical Co | Stable solvent compositions |
| US2999886A (en) * | 1959-11-13 | 1961-09-12 | Dow Chemical Co | Stable solvent compositions |
Also Published As
| Publication number | Publication date |
|---|---|
| GB401210A (en) | 1933-11-09 |
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