natgillin/translations-raw huggingface dataset:
It consists of hydrocarbons having carbon numbers predominantly in the range of C1 through C4 and boiling in the range of approximately minus 164 oC to minus 0.5 oC (-263oF to 31oF).]
It consists of hydrocarbons having carbon numbers predominantly in the range of C1 through C4 and boiling in the range of approximately minus 164 oC to minus 0.5 oC (-263 oF to 31 oF).]
[A complex combination of hydrocarbons obtained by subjecting hydrocarbon gases to a sweetening process to convert mercaptans or to remove acidic impurities.
[A complex combination of hydrocarbons obtained by subjecting hydrocarbon gases to a sweetening process to convert mercaptans or to remove acidic impurities.
[A complex combination of hydrocarbons having carbon numbers predominantly in the range of C1 through C3 and boiling in the range of approximately minus 164 oC to minus 42 oC (-263oF to - 44oF).]
[A complex combination of hydrocarbons having carbon numbers predominantly in the range of C1 through C3 and boiling in the range of approximately minus 164 oC to minus 42 oC (-263 oF to - 44 oF).]
[A complex combination of hydrocarbons produced by the distillation of crude oil and/or the cracking of tower gas oil.
[A complex combination of hydrocarbons produced by the distillation of crude oil and/or the cracking of tower gas oil.
[A complex combination of hydrocarbons produced by the catalytic cracking of gas oil.
[A complex combination of hydrocarbons produced by the catalytic cracking of gas oil.
[A complex combination obtained from various processes.
[A complex combination obtained from various processes.
[A complex combination of hydrocarbons produced by the fractionation of crude oil.
[A complex combination of hydrocarbons produced by the fractionation of crude oil.
[A complex combination of hydrocarbons obtained by the fractionation of combined naphtha streams.
[A complex combination of hydrocarbons obtained by the fractionation of combined naphtha streams.
[A complex combination of hydrocarbons obtained by the fractionation of light straight-run gasoline.
[A complex combination of hydrocarbons obtained by the fractionation of light straight-run gasoline.
[A complex combination of hydrocarbons produced by a naphtha unifiner desulfurization process and stripped from the naphtha product.
[A complex combination of hydrocarbons produced by a naphtha unifiner desulfurization process and stripped from the naphtha product.
[A complex combination of hydrocarbons obtained by the catalytic reforming of straight-run naphtha and fractionation of the total effluent.
[A complex combination of hydrocarbons obtained by the catalytic reforming of straight-run naphtha and fractionation of the total effluent.
[A complex combination of hydrocarbons produced by the fractionation of the charge to the C3 -C4 splitter.
[A complex combination of hydrocarbons produced by the fractionation of the charge to the C3 -C4 splitter.
[A complex combination of hydrocarbons obtained from the fractionation of the liquid from the first tower used in the distillation of crude oil.
[A complex combination of hydrocarbons obtained from the fractionation of the liquid from the first tower used in the distillation of crude oil.
[A complex combination of hydrocarbons obtained from fractionation of catalytic cracked naphtha.
[A complex combination of hydrocarbons obtained from fractionation of catalytic cracked naphtha.
[A complex combination of hydrocarbons obtained by the fractionation of catalytic cracked naphtha and distillate.
[A complex combination of hydrocarbons obtained by the fractionation of catalytic cracked naphtha and distillate.
[A complex combination of hydrocarbons obtained from the separation of thermal-cracked distillates, naphtha and gas oil.
[A complex combination of hydrocarbons obtained from the separation of thermal-cracked distillates, naphtha and gas oil.
[A complex combination of hydrocarbons obtained from the fractionation stabilization of thermal cracked hydrocarbons from petroleum coking process.
[A complex combination of hydrocarbons obtained from the fractionation stabilization of thermal cracked hydrocarbons from petroleum coking process.
[A complex combination of hydrocarbons produced by the distillation of products from a thermal cracking process, It consists of hydrocarbons having a carbon number predominantly of C4.]
[A complex combination of hydrocarbons produced by the distillation of products from a thermal cracking process, It consists of hydrocarbons having a carbon number predominantly of C4.]
[A complex combination of hydrocarbons obtained by the catalytic reforming of straight-run naphtha and the fractionation of the total effluent.
[A complex combination of hydrocarbons obtained by the catalytic reforming of straight-run naphtha and the fractionation of the total effluent.
[A complex combination of hydrocarbons produced by the distillation of products from a steam cracking process.
[A complex combination of hydrocarbons produced by the distillation of products from a steam cracking process.
It consists predominantly of propylene with some propane and boils in the range of approximately - 70 oC to 0 oC (-94oF to 32oF).]
It consists predominantly of propylene with some propane and boils in the range of approximately - 70 oC to 0 oC (-94 oF to 32 oF).]
[A complex combination of hydrocarbons produced by the distillation of the products of a steam cracking process.
[A complex combination of hydrocarbons produced by the distillation of the products of a steam cracking process.
[A complex combination of hydrocarbons obtained by subjecting a liquified petroleum gas mix to a sweetening process to oxidize mercaptans or to remove acidic impurities.
[A complex combination of hydrocarbons obtained by subjecting a liquified petroleum gas mix to a sweetening process to oxidize mercaptans or to remove acidic impurities.
[A complex combination of hydrocarbons obtained by recycling the gases of the benzene unit.
[A complex combination of hydrocarbons obtained by recycling the gases of the benzene unit.
[A complex combination of hydrocarbons obtained by distillation of a blend oil.
[A complex combination of hydrocarbons obtained by distillation of a blend oil.
[A complex combination of hydrocarbons obtained from stabilization of catalytic reformed naphtha.
[A complex combination of hydrocarbons obtained from stabilization of catalytic reformed naphtha.
[A complex combination of hydrocarbons produced by distillation of products from catalytic reforming of C6-C8 feed and recycled to conserve hydrogen.
[A complex combination of hydrocarbons produced by distillation of products from catalytic reforming of C6-C8 feed and recycled to conserve hydrogen.
[A complex combination of hydrocarbons produced by distillation of products from catalytic reforming of C6-C8feed.
[A complex combination of hydrocarbons produced by distillation of products from catalytic reforming of C6-C8 feed.
[A complex combination of hydrocarbons obtained by the extraction of hydrogen from a gas stream which consists primarily of hydrogen with small amounts of nitrogen, carbon monoxide, methane, ethane, and ethylene.
[A complex combination of hydrocarbons obtained by the extraction of hydrogen from a gas stream which consists primarily of hydrogen with small amounts of nitrogen, carbon monoxide, methane, ethane, and ethylene.
[The complex combination of dry gases from a gas concentration unit.
[The complex combination of dry gases from a gas concentration unit.
[A complex combination of hydrocarbons produced by distillation of products from combined gas streams in a gas concentration reabsorber.
[A complex combination of hydrocarbons produced by distillation of products from combined gas streams in a gas concentration reabsorber.
[A complex combination obtained by absorbing hydrogen from a hydrogen rich stream.
[A complex combination obtained by absorbing hydrogen from a hydrogen rich stream.
[A complex combination separated as a gas from hydrocarbon gases by chilling.
[A complex combination separated as a gas from hydrocarbon gases by chilling.
[A complex combination obtained from recycled hydrotreated blend oil.
[A complex combination obtained from recycled hydrotreated blend oil.
[A complex combination obtained from recycled reactor gases.
[A complex combination obtained from recycled reactor gases.
[A complex combination obtained from the reformers.
[A complex combination obtained from the reformers.
[A complex combination obtained from the reforming hydrotreating process.
[A complex combination obtained from the reforming hydrotreating process.
[A complex combination produced by distillation of products from a thermal cracking process.
[A complex combination produced by distillation of products from a thermal cracking process.
[A complex combination of hydrocarbons obtained from refractionation of products from a catalytic cracking process.
[A complex combination of hydrocarbons obtained from refractionation of products from a catalytic cracking process.
[A complex combination of hydrocarbons obtained from the catalytic reforming of straight run naphtha.
[A complex combination of hydrocarbons obtained from the catalytic reforming of straight run naphtha.
[A complex combination of hydrocarbons obtained from the stabilization of catalytic reformed naphtha.
[A complex combination of hydrocarbons obtained from the stabilization of catalytic reformed naphtha.
[A complex combination of hydrocarbons obtained by treating cracked distillates with hydrogen in the presence of a catalyst.
[A complex combination of hydrocarbons obtained by treating cracked distillates with hydrogen in the presence of a catalyst.
[A complex combination of hydrocarbons obtained from hydrodesulfurization of straight-run naphtha.
[A complex combination of hydrocarbons obtained from hydrodesulfurization of straight-run naphtha.
[A complex combination of hydrocarbons obtained from the catalytic reforming of straight-run naphtha followed by fractionation of the total effluent.
[A complex combination of hydrocarbons obtained from the catalytic reforming of straight-run naphtha followed by fractionation of the total effluent.
[A complex combination produced by the high-pressure flashing of the effluent from the reforming reactor.
[A complex combination produced by the high-pressure flashing of the effluent from the reforming reactor.
[A complex combination produced by low-pressure flashing of the effluent from the reforming reactor.
[A complex combination produced by low-pressure flashing of the effluent from the reforming reactor.
[A complex combination separated by distillation of a gas stream containing hydrogen, carbon monoxide, carbon dioxide and hydrocarbons having carbon numbers in the range of C1 through C6 or obtained by cracking ethane and propane.
[A complex combination separated by distillation of a gas stream containing hydrogen, carbon monoxide, carbon dioxide and hydrocarbons having carbon numbers in the range of C1 through C6 or obtained by cracking ethane and propane.
[A complex combination produced by treating the feed from the benzene unit with hydrogen in the presence of a catalyst followed by depentanizing.
[A complex combination produced by treating the feed from the benzene unit with hydrogen in the presence of a catalyst followed by depentanizing.
[A complex combination produced by the fractionation of the overhead products from the catalytic cracking process in the fluidized catalytic cracker.
[A complex combination produced by the fractionation of the overhead products from the catalytic cracking process in the fluidized catalytic cracker.
[A complex combination which consists primarily of hydrogen with various small amounts of methane, ethane, and propane.]
[A complex combination which consists primarily of hydrogen with various small amounts of methane, ethane, and propane.]
[A complex combination obtained by the liquid-vapor separation of the hydrocracking process reactor effluent.
[A complex combination obtained by the liquid-vapor separation of the hydrocracking process reactor effluent.
[A complex combination obtained from various petroleum refining operations.
[A complex combination obtained from various petroleum refining operations.
[A complex combination obtained from the chemical reforming of naphthenes to aromatics.
[A complex combination obtained from the chemical reforming of naphthenes to aromatics.
[A complex combination obtained from the flash drum of the unit treating sour kerosine with hydrogen in the presence of a catalyst.
[A complex combination obtained from the flash drum of the unit treating sour kerosine with hydrogen in the presence of a catalyst.
[A complex combination stripped from the liquid product of the unifiner desulfurization process.
[A complex combination stripped from the liquid product of the unifiner desulfurization process.
[A complex combination produced by the fractionation of the overhead product of the fluidized catalytic cracking process.
[A complex combination produced by the fractionation of the overhead product of the fluidized catalytic cracking process.
[A complex combination produced by scrubbing the overhead gas from the fluidized catalytic cracker.
[A complex combination produced by scrubbing the overhead gas from the fluidized catalytic cracker.
A complex combination obtained from viscosity reduction of residues in a furnace.
A complex combination obtained from viscosity reduction of residues in a furnace.
It consists of hydrocarbons having carbon numbers in the range of C3 through C4, predominantly of propane and propylene, and boiling in the range of approximately - 51 oC to - 1 oC (-60oF to 30oF.)]
It consists of hydrocarbons having carbon numbers in the range of C3 through C4, predominantly of propane and propylene, and boiling in the range of approximately - 51 oC to - 1 oC (-60 oF to 30 oF.)]
It consists of hydrocarbons having carbon numbers predominantly in the range of C3 through C5 and boiling in the range of approximately - 48 oC to 32 oC (-54oF to 90oF).]
It consists of hydrocarbons having carbon numbers predominantly in the range of C3 through C5 and boiling in the range of approximately - 48 oC to 32 oC (-54 oF to 90 oF).]
It consists of hydrocarbons having carbon numbers predominantly in the range of C3 through C7 and boiling in the range of approximately - 40 oC to 80 oC (-40 oF to 176 oF).]
It consists of hydrocarbons having carbon numbers predominantly in the range of C3 through C7 and boiling in the range of approximately - 40 oC to 80 oC (-40 oF to 176 oF).]
Gasoil – unspecified; [A complex combination of hydrocarbons from the distillation of catalytic reformer fracftionator residue.
Gasoil — unspecified; [A complex combination of hydrocarbons from the distillation of catalytic reformer fracftionator residue.
It consists predominantly of saturated aliphatic hydrocarbons having carbon numbers predominantly in the range of C4 through C8 and boiling in the range of approximately minus 20 oC to 120 oC (-4oF to 248oF).]
It consists predominantly of saturated aliphatic hydrocarbons having carbon numbers predominantly in the range of C4 through C8 and boiling in the range of approximately minus 20 oC to 120 oC (-4 oF to 248 oF).]
It consists of hydrocarbons having carbon numbers predominantly in the range of C5 through C6 and boiling in the range of approximately 100 oC to 200 oC (212oF to 392oF).]]
It consists of hydrocarbons having carbon numbers predominantly in the range of C5 through C6 and boiling in the range of approximately 100 oC to 200 oC (212 oF to 392 oF).]
It consists of hydrocarbons having carbon numbers predominantly in the range of C4 through C11 and boiling in the range of approximately minus 20 oC to 220 oC (-4oF to 428oF).]
It consists of hydrocarbons having carbon numbers predominantly in the range of C4 through C11 and boiling in the range of approximately minus 20 oC to 220 oC (-4 oF to 428 oF).]
It consists predominantly of aliphatic hydrocarbons having carbon numbers predominantly in the range of C4 through C10 and boiling in the range of approximately minus 20 oC to 180 oC (-4oF to 356oF).]
It consists predominantly of aliphatic hydrocarbons having carbon numbers predominantly in the range of C4 through C10 and boiling in the range of approximately minus 20 oC to 180 oC (-4 oF to 356 oF).]
It consists of hydrocarbons having carbon numbers predominantly in the range of C2 through C7 and boiling in the range of approximately - 88 oC to 99 oC (-127oF to 210oF).]
It consists of hydrocarbons having carbon numbers predominantly in the range of C2 through C7 and boiling in the range of approximately - 88 oC to 99 oC (-127 oF to 210 oF).]
It consists of hydrocarbons having carbon numbers predominantly in the range of C4 through C11 and boiling in the range of approximately minus 20 oC to 190 oC (-4oF to 374oF).
It consists of hydrocarbons having carbon numbers predominantly in the range of C4 through C11 and boiling in the range of approximately minus 20 oC to 190 oC (-4 oF to 374 oF).
It consists predominantly of hydrocarbons boiling in a range of approxim-ately 35 oC to 210 oC (95oF to 410oF).]
It consists predominantly of hydrocarbons boiling in a range of approxim-ately 35 oC to 210 oC (95 oF to 410 oF).]
This stream may contain 10 vol. % or more benzene.]]
This stream may contain 10 vol. % or more benzene.]
This stream may contain 10 vol.% or more benzene.]
This stream may contain 10 vol. % or more benzene.]
It consists predominantly of hydrocarbons having carbon numbers predominantly in the range of C5 through C12.]]
It consists predominantly of hydrocarbons having carbon numbers predominantly in the range of C5 through C12.]
It consists predominantly of aromatic hydrocarbons having carbon numbers predominantly in the range of C7 through C12 and boiling in the range of approximately 130 oC to 220 oC (266oF to 428oF).]]
It consists predominantly of aromatic hydrocarbons having carbon numbers predominantly in the range of C7 through C12 and boiling in the range of approximately 130 oC to 220 oC (266 oF to 428 oF).]
Naphtha (petroleum), hydrodesulfurized light, dearomatized; Low boiling point naphtha – unspecified;
Naphtha (petroleum), hydrodesulfurized light, dearomatized; Low boiling point naphtha — unspecified;
Hydrocarbons, C ≥ 5, C5-6-rich;
Hydrocarbons, C ≥ 5, C5-6-rich;
Solvent naphtha (petroleum), heavy arom.; Kerosine – unspecified;
Solvent naphtha (petroleum), heavy arom.; Kerosine — unspecified;
It consists predominantly of hydrocarbons having carbon numbers predominantly in the range of C13 through C27 and boiling in the range of approximately 240 oC to 400 oC (464oF to 752oF.]
It consists predominantly of hydrocarbons having carbon numbers predominantly in the range of C13 through C27 and boiling in the range of approximately 240 oC to 400 oC (464 oF to 752 oF.]
Lubricating oils (petroleum), C >25, solvent-extd., deasphalted, dewaxed, hydrogenated;
Lubricating oils (petroleum), C >25, solvent-extd., deasphalted, dewaxed, hydrogenated;
benzyl violet 4B; α-[4-(4-dimethylamino-α-4-[ethyl(3-sodiosulphonatobenzylamino] phenylbenzylidene)cyclohexa-2,5-dienylidene(ethyl)ammonio]toluene-3-sulphonate
benzyl violet 4B; α-[4-(4-dimethylamino-α-4-[ethyl(3-sodiosulphonatobenzyl)amino] phenylbenzylidene)cyclohexa-2,5-dienylidene(ethyl)ammonio]toluene-3-sulphonate
R: 45-48/23 S: 53-45
R: 45-48/23 S: 53-45
F; Xi; N
Xi; N
O; C; N
C; N
Úř. věst. C 146 A, 15.6.1990.
OJ C 146A, 15.6.1990.
Viz poznámka U v oddíle 1.1.3.
see Note U in 1.1.3.
Tabulka pro převod klasifikace podle směrnice 67/548/EHS na klasifikaci podle tohoto nařízení
Translation table from classification under Directive 67/548/EEC to classification under this Regulation
Tato příloha obsahuje tabulku pro usnadnění převodu klasifikace pro látku nebo směs podle směrnice 67/548/EHS nebo směrnice 1999/45/ES na odpovídající klasifikaci podle tohoto nařízení.
This Annex includes a table to assist translation of a classification made for a substance or a mixture under Directive 67/548/EEC or Directive 1999/45/EC, respectively, into the corresponding classification under this Regulation.
Jsou-li k dispozici údaje o dané látce nebo směsi, provede se hodnocení a klasifikace v souladu s články 9 až 13 tohoto nařízení.
Whenever data for the substance or mixture are available, an evaluation and classification shall be done in accordance with Articles 9 to13 of this Regulation.
Převodní tabulka
Translation table
Použité kódy jsou zavedeny v tabulce 1.1 a oddíle 1.1.2.2 přílohy VI.
The codes used are introduced in Table 1.1 and section 1.1.2.2 of Annex VI.
Převod mezi klasifikací podle směrnice 67/548/EHS a tímto nařízením
Translation between classification in accordance with Directive 67/548/EEC and this Regulation
Pro tyto třídy lze použít doporučenou minimální klasifikaci, jak je definována v oddíle 1.2.1.1 přílohy VI.
For these classes it is possible to use the recommended minimum classification as defined in section 1.2.1.1 in Annex VI.
K dispozici mohou být údaje nebo jiné informace, z nichž vyplývá, že je vhodné překlasifikování do přísnější kategorie.
Data or other information may be available to indicate that re-classification in a more severe category is appropriate.
Doporučuje se zařazení do kategorie 1B, ačkoliv je možné, že v některých případech by mohla být použitelná kategorie 1C.
It is recommended to classify in Category 1B even if it also could be possible that 1C could be applicable for certain cases.
Návrat k původním údajům nemusí vést k možnému rozlišení mezi kategoriemi 1B a 1C, jelikož doba expozice byla podle nařízení (ES) č. 440/2008 obvykle do 4 hodin.
Going back to original data, may not result in a possibility to distinguish between Category 1B or 1C, since the exposure period has normally been up to 4 hours according to Regulation (EC) No 440/2008.
V budoucnu by se však v případě, že údaje jsou odvozeny ze zkoušek dodržujících koncepci postupného zkoušení stanovenou v nařízení (ES) č. 440/2008, mohla uvážit kategorie 1C.
However, for the future, when data are derived from tests following a sequential approach as foreseen in the Regulation (EC) No 440/2008, Category 1C should be considered.
Ke standardní větě o nebezpečnosti lze připojit cestu expozice, je-li přesvědčivě prokázáno, že žádné jiné cesty expozice nevyvolávají nebezpečí.
The route of exposure could be added to the hazard statement if it is conclusively proven that no other routes of exposure cause the hazard.
Poznámka 4
Note 4
Standardní věty o nebezpečnosti H360 a H361 udávají pro účinky na sexuální funkci a plodnost a účinky na vývoj potomstva obecnou informaci: „Může poškodit reprodukční schopnost nebo plod v těle matky/Podezření na poškození reprodukční schopnosti nebo plodu v těle matky“.
Hazard statements H360 and H361 indicate a general concern for both the reproductive properties related to fertility and developmental effects; ‘May damage/Suspected of damaging fertility or the unborn child’.
Podle klasifikačních kritérií (oddíl 3.7 přílohy I) lze obecnou standardní větu o nebezpečnosti nahradit standardní větou o nebezpečnosti, která udává pouze jednu vlastnost, pokud se prokáže, že jeden z obou uvedených účinků není relevantní.
According to the classification criteria (Annex I, section 3.7) the general hazard statement can be replaced by the hazard statement indicating only the property of concern, in case either fertility or developmental effects are proven to be not relevant.
Klasifikace podle směrnice 67/548/EHS
Classification under Directive 67/548/EEC
Fyzikální stav látky, je-li důležitý
Physical state of the substance when relevant
Klasifikace podle tohoto nařízení
Classification under this Regulation
Třída a kategorie nebezpečnosti
Hazard Class-and-Category
Standardní věta o nebezpečnosti
Hazard statement
Přímý převod není možný.
No direct translation possible.
plyn
gas
kapalina, tuhá látka
liquid, solid
kapalina
liquid
tuhá látka
solid
Správný převod R10 pro kapaliny je
Correct translation of R10, liquid is:
1, H224, pokud je bod vzplanutí < 23 oC a počáteční bod varu ≤ 35 oC
1, H224 if flashpoint < 23 oC and initial boiling point ≤ 35 oC
2, H225, pokud je bod vzplanutí < 23 oC a počáteční bod varu > 35 oC
2, H225 if flashpoint < 23 oC and initial boiling point > 35 oC
3, H226, pokud je bod vzplanutí ≥ 23 oC
3, H226 if flashpoint ≥ 23 oC