BE413723A - - Google Patents
Info
- Publication number
- BE413723A BE413723A BE413723DA BE413723A BE 413723 A BE413723 A BE 413723A BE 413723D A BE413723D A BE 413723DA BE 413723 A BE413723 A BE 413723A
- Authority
- BE
- Belgium
- Prior art keywords
- molecular weight
- alcohols
- high molecular
- temperature
- unsaturated aliphatic
- Prior art date
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- RWSOTUBLDIXVET-UHFFFAOYSA-N dihydrogen sulfide Chemical compound S RWSOTUBLDIXVET-UHFFFAOYSA-N 0.000 claims description 10
- 150000001298 alcohols Chemical class 0.000 claims description 9
- 239000000203 mixture Substances 0.000 claims description 8
- 239000003054 catalyst Substances 0.000 claims description 7
- 125000001931 aliphatic group Chemical group 0.000 claims description 4
- 229910000037 hydrogen sulfide Inorganic materials 0.000 claims description 4
- 238000000034 method Methods 0.000 claims description 3
- 125000004432 carbon atoms Chemical group C* 0.000 claims description 2
- 230000000875 corresponding Effects 0.000 claims description 2
- 238000004519 manufacturing process Methods 0.000 claims description 2
- MCMNRKCIXSYSNV-UHFFFAOYSA-N ZrO2 Chemical compound O=[Zr]=O MCMNRKCIXSYSNV-UHFFFAOYSA-N 0.000 description 8
- 239000012043 crude product Substances 0.000 description 4
- OKTJSMMVPCPJKN-UHFFFAOYSA-N carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 3
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 3
- QSHDDOUJBYECFT-UHFFFAOYSA-N mercury Chemical compound [Hg] QSHDDOUJBYECFT-UHFFFAOYSA-N 0.000 description 3
- 229910052753 mercury Inorganic materials 0.000 description 3
- 229910052751 metal Inorganic materials 0.000 description 3
- 239000002184 metal Substances 0.000 description 3
- 239000000126 substance Substances 0.000 description 3
- LJLJPBMSWIYGOA-KTKRTIGZSA-N (Z)-octadec-9-ene-1-thiol Chemical compound CCCCCCCC\C=C/CCCCCCCCS LJLJPBMSWIYGOA-KTKRTIGZSA-N 0.000 description 2
- 239000007789 gas Substances 0.000 description 2
- XEEYBQQBJWHFJM-UHFFFAOYSA-N iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 2
- CPLXHLVBOLITMK-UHFFFAOYSA-N magnesium oxide Chemical compound [Mg]=O CPLXHLVBOLITMK-UHFFFAOYSA-N 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- PXHVJJICTQNCMI-UHFFFAOYSA-N nickel Chemical compound [Ni] PXHVJJICTQNCMI-UHFFFAOYSA-N 0.000 description 2
- IJGRMHOSHXDMSA-UHFFFAOYSA-N nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 2
- NBIIXXVUZAFLBC-UHFFFAOYSA-N phosphoric acid Chemical compound OP(O)(O)=O NBIIXXVUZAFLBC-UHFFFAOYSA-N 0.000 description 2
- 239000008262 pumice Substances 0.000 description 2
- 239000002994 raw material Substances 0.000 description 2
- 239000002893 slag Substances 0.000 description 2
- 239000007921 spray Substances 0.000 description 2
- 239000004575 stone Substances 0.000 description 2
- 150000004763 sulfides Chemical class 0.000 description 2
- GWEVSGVZZGPLCZ-UHFFFAOYSA-N titan oxide Chemical compound O=[Ti]=O GWEVSGVZZGPLCZ-UHFFFAOYSA-N 0.000 description 2
- ZENZJGDPWWLORF-KTKRTIGZSA-N (Z)-octadec-9-enal Chemical compound CCCCCCCC\C=C/CCCCCCCC=O ZENZJGDPWWLORF-KTKRTIGZSA-N 0.000 description 1
- 229910052684 Cerium Inorganic materials 0.000 description 1
- BXWNKGSJHAJOGX-UHFFFAOYSA-N Cetyl alcohol Chemical compound CCCCCCCCCCCCCCCCO BXWNKGSJHAJOGX-UHFFFAOYSA-N 0.000 description 1
- LQZZUXJYWNFBMV-UHFFFAOYSA-N Dodecanol Chemical compound CCCCCCCCCCCCO LQZZUXJYWNFBMV-UHFFFAOYSA-N 0.000 description 1
- ALSTYHKOOCGGFT-KTKRTIGZSA-N Oleyl alcohol Chemical compound CCCCCCCC\C=C/CCCCCCCCO ALSTYHKOOCGGFT-KTKRTIGZSA-N 0.000 description 1
- 229910052776 Thorium Inorganic materials 0.000 description 1
- 229910052770 Uranium Inorganic materials 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- PNEYBMLMFCGWSK-UHFFFAOYSA-N al2o3 Chemical compound [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 description 1
- 229910000147 aluminium phosphate Inorganic materials 0.000 description 1
- 229910052788 barium Inorganic materials 0.000 description 1
- DSAJWYNOEDNPEQ-UHFFFAOYSA-N barium(0) Chemical compound [Ba] DSAJWYNOEDNPEQ-UHFFFAOYSA-N 0.000 description 1
- ATBAMAFKBVZNFJ-UHFFFAOYSA-N beryllium(0) Chemical compound [Be] ATBAMAFKBVZNFJ-UHFFFAOYSA-N 0.000 description 1
- 238000004061 bleaching Methods 0.000 description 1
- 238000009835 boiling Methods 0.000 description 1
- BDOSMKKIYDKNTQ-UHFFFAOYSA-N cadmium Chemical compound [Cd] BDOSMKKIYDKNTQ-UHFFFAOYSA-N 0.000 description 1
- 229910052793 cadmium Inorganic materials 0.000 description 1
- OYPRJOBELJOOCE-UHFFFAOYSA-N calcium Chemical compound [Ca] OYPRJOBELJOOCE-UHFFFAOYSA-N 0.000 description 1
- 229910052791 calcium Inorganic materials 0.000 description 1
- 239000011575 calcium Substances 0.000 description 1
- CURLTUGMZLYLDI-UHFFFAOYSA-N carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 1
- 229910002092 carbon dioxide Inorganic materials 0.000 description 1
- 239000001569 carbon dioxide Substances 0.000 description 1
- 239000000969 carrier Substances 0.000 description 1
- GWXLDORMOJMVQZ-UHFFFAOYSA-N cerium Chemical compound [Ce] GWXLDORMOJMVQZ-UHFFFAOYSA-N 0.000 description 1
- 229960000541 cetyl alcohol Drugs 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 229910052804 chromium Inorganic materials 0.000 description 1
- VYZAMTAEIAYCRO-UHFFFAOYSA-N chromium Chemical compound [Cr] VYZAMTAEIAYCRO-UHFFFAOYSA-N 0.000 description 1
- 239000011651 chromium Substances 0.000 description 1
- 239000000571 coke Substances 0.000 description 1
- 238000004040 coloring Methods 0.000 description 1
- 229910052802 copper Inorganic materials 0.000 description 1
- 239000010949 copper Substances 0.000 description 1
- RYGMFSIKBFXOCR-UHFFFAOYSA-N copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 1
- 235000014113 dietary fatty acids Nutrition 0.000 description 1
- 238000004821 distillation Methods 0.000 description 1
- WNAHIZMDSQCWRP-UHFFFAOYSA-N dodecane-1-thiol Chemical compound CCCCCCCCCCCCS WNAHIZMDSQCWRP-UHFFFAOYSA-N 0.000 description 1
- 238000004043 dyeing Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 239000000194 fatty acid Substances 0.000 description 1
- 150000004665 fatty acids Chemical class 0.000 description 1
- 230000002349 favourable Effects 0.000 description 1
- 239000000499 gel Substances 0.000 description 1
- 239000011521 glass Substances 0.000 description 1
- 125000005456 glyceride group Chemical group 0.000 description 1
- 239000010439 graphite Substances 0.000 description 1
- 229910002804 graphite Inorganic materials 0.000 description 1
- 150000004820 halides Chemical class 0.000 description 1
- 238000005984 hydrogenation reaction Methods 0.000 description 1
- 239000011261 inert gas Substances 0.000 description 1
- 229910052500 inorganic mineral Inorganic materials 0.000 description 1
- 239000011630 iodine Substances 0.000 description 1
- PNDPGZBMCMUPRI-UHFFFAOYSA-N iodine Chemical compound II PNDPGZBMCMUPRI-UHFFFAOYSA-N 0.000 description 1
- 229910052740 iodine Inorganic materials 0.000 description 1
- 229910052742 iron Inorganic materials 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- FYYHWMGAXLPEAU-UHFFFAOYSA-N magnesium Chemical compound [Mg] FYYHWMGAXLPEAU-UHFFFAOYSA-N 0.000 description 1
- 229910052749 magnesium Inorganic materials 0.000 description 1
- 239000011777 magnesium Substances 0.000 description 1
- 239000000395 magnesium oxide Substances 0.000 description 1
- PWHULOQIROXLJO-UHFFFAOYSA-N manganese Chemical compound [Mn] PWHULOQIROXLJO-UHFFFAOYSA-N 0.000 description 1
- 229910052748 manganese Inorganic materials 0.000 description 1
- 239000011572 manganese Substances 0.000 description 1
- 239000000155 melt Substances 0.000 description 1
- 150000002739 metals Chemical class 0.000 description 1
- 239000011707 mineral Substances 0.000 description 1
- ZOKXTWBITQBERF-UHFFFAOYSA-N molybdenum Chemical compound [Mo] ZOKXTWBITQBERF-UHFFFAOYSA-N 0.000 description 1
- 229910052750 molybdenum Inorganic materials 0.000 description 1
- 239000011733 molybdenum Substances 0.000 description 1
- 230000001264 neutralization Effects 0.000 description 1
- 229910052759 nickel Inorganic materials 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- 229940055577 oleyl alcohol Drugs 0.000 description 1
- 230000001590 oxidative Effects 0.000 description 1
- 235000021317 phosphate Nutrition 0.000 description 1
- 150000003013 phosphoric acid derivatives Chemical class 0.000 description 1
- OAICVXFJPJFONN-UHFFFAOYSA-N phosphorus Chemical compound [P] OAICVXFJPJFONN-UHFFFAOYSA-N 0.000 description 1
- 229910052698 phosphorus Inorganic materials 0.000 description 1
- 239000011574 phosphorus Substances 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 150000003839 salts Chemical class 0.000 description 1
- 150000004760 silicates Chemical class 0.000 description 1
- 239000011780 sodium chloride Substances 0.000 description 1
- CIOAGBVUUVVLOB-UHFFFAOYSA-N strontium Chemical compound [Sr] CIOAGBVUUVVLOB-UHFFFAOYSA-N 0.000 description 1
- 229910052712 strontium Inorganic materials 0.000 description 1
- 150000003467 sulfuric acid derivatives Chemical class 0.000 description 1
- ZSLUVFAKFWKJRC-UHFFFAOYSA-N thorium Chemical compound [Th] ZSLUVFAKFWKJRC-UHFFFAOYSA-N 0.000 description 1
- 229910052719 titanium Inorganic materials 0.000 description 1
- 239000010936 titanium Substances 0.000 description 1
- RTAQQCXQSZGOHL-UHFFFAOYSA-N titanium Chemical compound [Ti] RTAQQCXQSZGOHL-UHFFFAOYSA-N 0.000 description 1
- 239000004408 titanium dioxide Substances 0.000 description 1
- WFKWXMTUELFFGS-UHFFFAOYSA-N tungsten Chemical compound [W] WFKWXMTUELFFGS-UHFFFAOYSA-N 0.000 description 1
- 229910052721 tungsten Inorganic materials 0.000 description 1
- 239000010937 tungsten Substances 0.000 description 1
- JFALSRSLKYAFGM-UHFFFAOYSA-N uranium(0) Chemical compound [U] JFALSRSLKYAFGM-UHFFFAOYSA-N 0.000 description 1
- 229910052720 vanadium Inorganic materials 0.000 description 1
- LEONUFNNVUYDNQ-UHFFFAOYSA-N vanadium(0) Chemical compound [V] LEONUFNNVUYDNQ-UHFFFAOYSA-N 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
- 239000010457 zeolite Substances 0.000 description 1
- HCHKCACWOHOZIP-UHFFFAOYSA-N zinc Chemical compound [Zn] HCHKCACWOHOZIP-UHFFFAOYSA-N 0.000 description 1
- 229910052725 zinc Inorganic materials 0.000 description 1
- 239000011701 zinc Substances 0.000 description 1
- QCWXUUIWCKQGHC-UHFFFAOYSA-N zirconium Chemical compound [Zr] QCWXUUIWCKQGHC-UHFFFAOYSA-N 0.000 description 1
- 229910052726 zirconium Inorganic materials 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C319/00—Preparation of thiols, sulfides, hydropolysulfides or polysulfides
- C07C319/02—Preparation of thiols, sulfides, hydropolysulfides or polysulfides of thiols
- C07C319/04—Preparation of thiols, sulfides, hydropolysulfides or polysulfides of thiols by addition of hydrogen sulfide or its salts to unsaturated compounds
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Description
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Procédé pour préparer des mercaptans à poids moléculaire élevé.
On a trouvé qu'on obtient des mercaptans aliphatiques et cyclo-aliphatiques saturés et non saturés à poids moléculaire élevé en faisant passer les alcools à poids moléculaire élevé correspondants, à température élevée et en présence d'hydrogène sulfuré, sur des catalyseurs et en particulier sur ceux.qui ont une action déshydratante.
Comme matières premières pour le présent procédé on envisagera des alcools aliphatiques et cyclo-aliphatiques saturés et non saturés à poids moléculaire élevé renfermant au moins 12 atomes de carbone ou des mélanges de tels alcools.
On peut préparer ces alcools par exemple en oxydant des paraf.fines ou en hydrogénant les acides gras tirés de glycérides
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naturels.
Suivant l'usage envisagé pour le mélange de mercaptans escompté on peut également partir de mélanges d'alcools supérieurs et d'alcools inférieurs. La réaction s'effectuera avantageusement à des'températures comprises entre 150 et 450 C. et le cas échéant sous pression élevée ou réduite. A part les matières premières, des gaz ou des vapeurs inertes tels que l'azote, l'anhydride carbonique ou la vapeur d'eau peuvent aussi être présents. Au lieu d'hydrogène sulfuré pur on peut aussi employer des gaz en contenant de fortes proportions. Comme catalyseurs on envisagera un grand nombre de substances.
Des substances agissant d'une manière particulièrement favorable sont les déshydratants connus comme par exemple les oxydes et sels (phosphates, halogénures, sulfates ou sulfures) du glucinium, du magnésium, du calcium, du strontium, du baryum, du manganèse, du cadmium, du zinc, du cuivre, du nickel, du fer, du titane, du zirconium, du cérium, du thorium, du plomb, du phosphore, du vanadium, du chrome, du molybdène, du tungstène et dé l'uranium, qu'on emploiera soit isolément soit mélangés entre eux, le cas échéant sur des matières de grande surface ou sur des métaux, des minéraux ou des débris de poterie. Ces matières s'emploieront à titre de compléments sous forme soit broyée soit finement divisée d'autre manière ou'à titre de supports sous forme de grains ou de fragments.
On peut citer dans cet ordre d'idées par exemple les terres décolorantes alcalines, neutres et acides, les permutites, les zéolithes et autres silicates, la pierre ponce, les bauxites, les débris de terre cuite, la magnésie, le verre, les fils métalliques, les grenailles métalliques, les laitiers et scories, le coke, le graphite,
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les gels actifs et les charbons actifs.
Les mercaptans susceptibles d'être obtenus par le présent procédé conviennent surtout pour la préparation de substances auxiliaires de teinturerie et celle des colorants.
EXEMPLE 1
Sur du dioxyde de zirconium en granules faire passer à une température d'environ 320 C. un mélange de 1 partie en volume de vapeur d'alcool octodécylique et de 20 à 30 parties en volume d'hydrogène sulfuré. Le liquide ainsi obtenu, qui se solidifie progressivement dans le récipient, renferme 90% d'octodécyl-mercaptan en outre de . petites quantités d'octodécylène et de sulfure de dioctodécyle. Cet octodécyl-mercaptan bout à une température de 170 à 171 C. sous une pression de 1,5 mm..de mercure; il fond à une température de 34 à 35 C.
Au lieu de dioxyde de.zirconium granulé on peut aussi employer par exemple un mélange de dioxyde de zirconium et de pierre ponce pulvérisée. L'activité des catalyseurs ne s'affaiblit pas,méme âpres plusieurs semaines de service.
EXEMPLE 2
Faire passer à une température de 300 C. comme il est dit à l'exemple 1 un mélange de vapeur d'alcool octodécy- lique et d'hydrogène sulfuré sur du charbon actif qu'on aura traité au moyen d'acide phosphorique. Faire pour cela circuler l'hydrogène sulfuré en cycle fermé. Le produit brut isolé du gaz conduit en cycle fermé renferme environ 80% d'octodécyl-mercaptan.
EXEMPLE 3
Vaporiser de l'alcool tiré de l'huile de blanc
<Desc/Clms Page number 4>
de baleine (indice d'iode 68) dans un courant d'hydrogène sulfuré en excès et faire passer les vapeurs à une tempéra- ture d'environ 300 C sur un catalyseur à base d'oxyde d'aluminium. En distillant par fraction sous pression ré- duite le produit brut obtenu on obtient une fraction bouil- lant aux températures comprises entre 151 et 165 C. sous une pression de lmm. et qui renferme environ 91 à 92 % d'oléyl- mercaptan.
EXEMPLE 4
Vaporiser de l'alcool dodécylique dans un courant d'hydrogène sulfuré en excès et faire passer ces vapeurs à une température de 330 C. sur un catalyseur composé de dioxyde de titane en granules. Le produit brut susceptible d'être obtenu de cette manière se compose de 80% de dodécyl- mercaptan, qui bout aux températures comprises entre 95 et 100 C sous une pression de 1 mm. de mercure.
EXEMPLE 5
Sur un catalyseur tel que celui employé suivant l'exemple 1 faire passer à une température de 300 à 340 C. de l'alcool oléylique préparé par hydrogénation partielle de l'aldéhyde oléylique, cet alcool .étant mélangé avec quarante fois son volume d'hydrogène sulfuré. Le produit brut obtenu se compose de 80% d'oléyl-mercaptan.
EXEMPLE 6
Faire passer à une température de 320 C. un mélange d'alcool cétylique à l'état de vapeur et d'hydrogène sulfuré sur du dioxyde de zirconium en granules. On peut en recueil- lir la majeure partie par distillation sous pression réduite.
Il bout sous une pression de 0,8 mm. de mercure dans la zone de température comprise entre 140 et 155 C.
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Process for preparing high molecular weight mercaptans.
It has been found that high molecular weight saturated and unsaturated aliphatic and cycloaliphatic mercaptans are obtained by passing the corresponding high molecular weight alcohols, at elevated temperature and in the presence of hydrogen sulfide, over catalysts and in particular on those. which have a dehydrating action.
As raw materials for the present process, high molecular weight saturated and unsaturated aliphatic and cycloaliphatic alcohols containing at least 12 carbon atoms or mixtures of such alcohols will be contemplated.
These alcohols can be prepared, for example, by oxidizing paraffins or by hydrogenating fatty acids obtained from glycerides.
<Desc / Clms Page number 2>
natural.
Depending on the use envisaged for the mixture of mercaptans expected, it is also possible to start from mixtures of higher alcohols and lower alcohols. The reaction will advantageously be carried out at temperatures of between 150 and 450 ° C. and optionally under high or reduced pressure. Apart from raw materials, inert gases or vapors such as nitrogen, carbon dioxide or water vapor may also be present. Instead of pure hydrogen sulphide, it is also possible to use gases containing high proportions. A large number of substances will be considered as catalysts.
Substances which act in a particularly favorable manner are known dehydrating agents such as for example the oxides and salts (phosphates, halides, sulphates or sulphides) of glucinium, magnesium, calcium, strontium, barium, manganese, cadmium, zinc, copper, nickel, iron, titanium, zirconium, cerium, thorium, lead, phosphorus, vanadium, chromium, molybdenum, tungsten and uranium, which use either singly or mixed together, where appropriate on large surface materials or on metals, minerals or pottery debris. These materials will be used as supplements in either ground or finely divided form in other ways or as carriers in the form of grains or fragments.
In this order of ideas, we can cite, for example, alkaline, neutral and acid bleaching earths, permutites, zeolites and other silicates, pumice stone, bauxites, terracotta debris, magnesia, glass, wires metal, metal shot, slag and slag, coke, graphite,
<Desc / Clms Page number 3>
active gels and activated carbons.
The mercaptans obtainable by the present process are suitable above all for the preparation of auxiliary substances for dyeing and for coloring.
EXAMPLE 1
Pass a mixture of 1 part by volume of octodecyl alcohol vapor and 20 to 30 parts by volume of hydrogen sulphide over granular zirconium dioxide at a temperature of about 320 ° C.. The liquid thus obtained, which gradually solidifies in the container, contains 90% of octodecyl-mercaptan in addition to. small amounts of octodecylene and dioctodecyl sulfide. This octodecyl-mercaptan boils at a temperature of 170 to 171 ° C. under a pressure of 1.5 mm. Of mercury; it melts at a temperature of 34-35 C.
Instead of granulated zirconium dioxide, for example, a mixture of zirconium dioxide and powdered pumice stone can also be used. The activity of the catalysts does not weaken, even after several weeks of service.
EXAMPLE 2
Pass a temperature of 300 ° C. as described in Example 1 with a mixture of octodecyl alcohol vapor and hydrogen sulphide over activated carbon which has been treated with phosphoric acid. To do this, circulate the hydrogen sulphide in a closed cycle. The crude product isolated from the gas carried out in a closed cycle contains approximately 80% octodecyl-mercaptan.
EXAMPLE 3
Spray alcohol from white oil
<Desc / Clms Page number 4>
whalebone (iodine number 68) in a stream of excess hydrogen sulphide and pass the vapors at a temperature of about 300 ° C over an aluminum oxide catalyst. By fractionally distilling the crude product obtained under reduced pressure, a fraction boiling at temperatures between 151 and 165 ° C. under a pressure of 1 mm is obtained. and which contains about 91 to 92% oleyl mercaptan.
EXAMPLE 4
Spray dodecyl alcohol in a stream of excess hydrogen sulphide and pass these vapors at a temperature of 330 ° C. over a catalyst composed of granulated titanium dioxide. The crude product obtainable in this way consists of 80% dodecylmercaptan, which boils at temperatures between 95 and 100 ° C. under a pressure of 1 mm. of mercury.
EXAMPLE 5
On a catalyst such as that employed according to Example 1, pass oleyl alcohol prepared by partial hydrogenation of oleyl aldehyde at a temperature of 300 to 340 C., this alcohol being mixed with forty times its volume of. hydrogen sulfide. The crude product obtained consists of 80% oleyl-mercaptan.
EXAMPLE 6
Pass a mixture of cetyl alcohol in the vapor state and hydrogen sulfide at a temperature of 320 ° C. over granulated zirconium dioxide. Most of it can be collected by distillation under reduced pressure.
It boils under a pressure of 0.8 mm. of mercury in the temperature zone between 140 and 155 C.
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