UA81971C2 - Способ и устройство для получения дихлорпропанолов из глицерина - Google Patents
Способ и устройство для получения дихлорпропанолов из глицерина Download PDFInfo
- Publication number
- UA81971C2 UA81971C2 UAA200603528A UAA200603528A UA81971C2 UA 81971 C2 UA81971 C2 UA 81971C2 UA A200603528 A UAA200603528 A UA A200603528A UA A200603528 A UAA200603528 A UA A200603528A UA 81971 C2 UA81971 C2 UA 81971C2
- Authority
- UA
- Ukraine
- Prior art keywords
- reaction
- cascade
- distillation
- differs
- dichloropropanols
- Prior art date
Links
- PEDCQBHIVMGVHV-UHFFFAOYSA-N Glycerine Chemical compound OCC(O)CO PEDCQBHIVMGVHV-UHFFFAOYSA-N 0.000 title claims abstract description 93
- XEPXTKKIWBPAEG-UHFFFAOYSA-N 1,1-dichloropropan-1-ol Chemical class CCC(O)(Cl)Cl XEPXTKKIWBPAEG-UHFFFAOYSA-N 0.000 title claims abstract description 35
- 238000000034 method Methods 0.000 title claims abstract description 30
- 235000011187 glycerol Nutrition 0.000 title abstract description 32
- 238000006243 chemical reaction Methods 0.000 claims abstract description 40
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 29
- HUXDTFZDCPYTCF-UHFFFAOYSA-N 1-chloropropane-1,1-diol Chemical class CCC(O)(O)Cl HUXDTFZDCPYTCF-UHFFFAOYSA-N 0.000 claims abstract description 17
- 238000007038 hydrochlorination reaction Methods 0.000 claims abstract description 9
- 229940051269 1,3-dichloro-2-propanol Drugs 0.000 claims abstract description 5
- 239000007788 liquid Substances 0.000 claims abstract description 5
- ZXCYIJGIGSDJQQ-UHFFFAOYSA-N 2,3-dichloropropan-1-ol Chemical compound OCC(Cl)CCl ZXCYIJGIGSDJQQ-UHFFFAOYSA-N 0.000 claims abstract description 4
- 238000004821 distillation Methods 0.000 claims description 38
- QTBSBXVTEAMEQO-UHFFFAOYSA-N Acetic acid Natural products CC(O)=O QTBSBXVTEAMEQO-UHFFFAOYSA-N 0.000 claims description 32
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 claims description 21
- 239000011541 reaction mixture Substances 0.000 claims description 20
- 239000000047 product Substances 0.000 claims description 17
- 239000000203 mixture Substances 0.000 claims description 12
- 239000003054 catalyst Substances 0.000 claims description 10
- 239000002699 waste material Substances 0.000 claims description 8
- 238000005292 vacuum distillation Methods 0.000 claims description 7
- 238000009835 boiling Methods 0.000 claims description 5
- 238000012545 processing Methods 0.000 claims description 4
- DYPJJAAKPQKWTM-UHFFFAOYSA-N 2-chloropropane-1,3-diol Chemical compound OCC(Cl)CO DYPJJAAKPQKWTM-UHFFFAOYSA-N 0.000 claims description 2
- 239000007795 chemical reaction product Substances 0.000 claims description 2
- 238000012958 reprocessing Methods 0.000 claims description 2
- 239000002904 solvent Substances 0.000 claims description 2
- SSZWWUDQMAHNAQ-UHFFFAOYSA-N 3-chloropropane-1,2-diol Chemical compound OCC(O)CCl SSZWWUDQMAHNAQ-UHFFFAOYSA-N 0.000 claims 1
- 125000000218 acetic acid group Chemical group C(C)(=O)* 0.000 claims 1
- 150000001732 carboxylic acid derivatives Chemical class 0.000 claims 1
- DEWLEGDTCGBNGU-UHFFFAOYSA-N 1,3-dichloropropan-2-ol Chemical compound ClCC(O)CCl DEWLEGDTCGBNGU-UHFFFAOYSA-N 0.000 abstract description 5
- 230000003197 catalytic effect Effects 0.000 abstract description 4
- QQONPFPTGQHPMA-UHFFFAOYSA-N Propene Chemical compound CC=C QQONPFPTGQHPMA-UHFFFAOYSA-N 0.000 description 9
- BRLQWZUYTZBJKN-UHFFFAOYSA-N Epichlorohydrin Chemical compound ClCC1CO1 BRLQWZUYTZBJKN-UHFFFAOYSA-N 0.000 description 8
- 230000015572 biosynthetic process Effects 0.000 description 7
- 150000001875 compounds Chemical class 0.000 description 6
- 238000004519 manufacturing process Methods 0.000 description 6
- 239000012048 reactive intermediate Substances 0.000 description 6
- 238000000926 separation method Methods 0.000 description 6
- 238000002474 experimental method Methods 0.000 description 5
- 238000003786 synthesis reaction Methods 0.000 description 5
- XXROGKLTLUQVRX-UHFFFAOYSA-N allyl alcohol Chemical compound OCC=C XXROGKLTLUQVRX-UHFFFAOYSA-N 0.000 description 4
- 150000001735 carboxylic acids Chemical class 0.000 description 4
- 239000007789 gas Substances 0.000 description 4
- 239000002994 raw material Substances 0.000 description 4
- 239000000243 solution Substances 0.000 description 4
- 238000011144 upstream manufacturing Methods 0.000 description 4
- OSDWBNJEKMUWAV-UHFFFAOYSA-N Allyl chloride Chemical compound ClCC=C OSDWBNJEKMUWAV-UHFFFAOYSA-N 0.000 description 3
- ZAMOUSCENKQFHK-UHFFFAOYSA-N Chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 description 3
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 3
- 239000000460 chlorine Substances 0.000 description 3
- 229910052801 chlorine Inorganic materials 0.000 description 3
- 238000007033 dehydrochlorination reaction Methods 0.000 description 3
- 238000005516 engineering process Methods 0.000 description 3
- DURPTKYDGMDSBL-UHFFFAOYSA-N 1-butoxybutane Chemical compound CCCCOCCCC DURPTKYDGMDSBL-UHFFFAOYSA-N 0.000 description 2
- MHAJPDPJQMAIIY-UHFFFAOYSA-N Hydrogen peroxide Chemical compound OO MHAJPDPJQMAIIY-UHFFFAOYSA-N 0.000 description 2
- 239000002253 acid Substances 0.000 description 2
- 239000006227 byproduct Substances 0.000 description 2
- 238000005660 chlorination reaction Methods 0.000 description 2
- MVPPADPHJFYWMZ-UHFFFAOYSA-N chlorobenzene Chemical compound ClC1=CC=CC=C1 MVPPADPHJFYWMZ-UHFFFAOYSA-N 0.000 description 2
- XBDQKXXYIPTUBI-UHFFFAOYSA-N dimethylselenoniopropionate Natural products CCC(O)=O XBDQKXXYIPTUBI-UHFFFAOYSA-N 0.000 description 2
- IXCSERBJSXMMFS-UHFFFAOYSA-N hydrogen chloride Substances Cl.Cl IXCSERBJSXMMFS-UHFFFAOYSA-N 0.000 description 2
- 229910000041 hydrogen chloride Inorganic materials 0.000 description 2
- 239000007791 liquid phase Substances 0.000 description 2
- 230000003647 oxidation Effects 0.000 description 2
- 238000007254 oxidation reaction Methods 0.000 description 2
- HVAMZGADVCBITI-UHFFFAOYSA-M pent-4-enoate Chemical compound [O-]C(=O)CCC=C HVAMZGADVCBITI-UHFFFAOYSA-M 0.000 description 2
- 238000000746 purification Methods 0.000 description 2
- 238000011084 recovery Methods 0.000 description 2
- 238000005507 spraying Methods 0.000 description 2
- 239000007858 starting material Substances 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- WSLDOOZREJYCGB-UHFFFAOYSA-N 1,2-Dichloroethane Chemical compound ClCCCl WSLDOOZREJYCGB-UHFFFAOYSA-N 0.000 description 1
- KNKRKFALVUDBJE-UHFFFAOYSA-N 1,2-dichloropropane Chemical compound CC(Cl)CCl KNKRKFALVUDBJE-UHFFFAOYSA-N 0.000 description 1
- 239000000853 adhesive Substances 0.000 description 1
- 230000001070 adhesive effect Effects 0.000 description 1
- 239000011260 aqueous acid Substances 0.000 description 1
- 239000007864 aqueous solution Substances 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- AXCZMVOFGPJBDE-UHFFFAOYSA-L calcium dihydroxide Chemical compound [OH-].[OH-].[Ca+2] AXCZMVOFGPJBDE-UHFFFAOYSA-L 0.000 description 1
- 239000000920 calcium hydroxide Substances 0.000 description 1
- 229910001861 calcium hydroxide Inorganic materials 0.000 description 1
- 238000004364 calculation method Methods 0.000 description 1
- 238000003889 chemical engineering Methods 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 239000003822 epoxy resin Substances 0.000 description 1
- 238000000605 extraction Methods 0.000 description 1
- 150000004820 halides Chemical class 0.000 description 1
- LNEPOXFFQSENCJ-UHFFFAOYSA-N haloperidol Chemical compound C1CC(O)(C=2C=CC(Cl)=CC=2)CCN1CCCC(=O)C1=CC=C(F)C=C1 LNEPOXFFQSENCJ-UHFFFAOYSA-N 0.000 description 1
- 231100001261 hazardous Toxicity 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 230000007062 hydrolysis Effects 0.000 description 1
- 238000006460 hydrolysis reaction Methods 0.000 description 1
- 150000002432 hydroperoxides Chemical class 0.000 description 1
- QWPPOHNGKGFGJK-UHFFFAOYSA-N hypochlorous acid Chemical compound ClO QWPPOHNGKGFGJK-UHFFFAOYSA-N 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 238000009776 industrial production Methods 0.000 description 1
- 239000012442 inert solvent Substances 0.000 description 1
- 230000003993 interaction Effects 0.000 description 1
- 230000014759 maintenance of location Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 239000003960 organic solvent Substances 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 229920000647 polyepoxide Polymers 0.000 description 1
- 239000002244 precipitate Substances 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 235000019260 propionic acid Nutrition 0.000 description 1
- 125000004805 propylene group Chemical group [H]C([H])([H])C([H])([*:1])C([H])([H])[*:2] 0.000 description 1
- IUVKMZGDUIUOCP-BTNSXGMBSA-N quinbolone Chemical compound O([C@H]1CC[C@H]2[C@H]3[C@@H]([C@]4(C=CC(=O)C=C4CC3)C)CC[C@@]21C)C1=CCCC1 IUVKMZGDUIUOCP-BTNSXGMBSA-N 0.000 description 1
- 150000003839 salts Chemical class 0.000 description 1
- 238000003860 storage Methods 0.000 description 1
- 229920003051 synthetic elastomer Polymers 0.000 description 1
- 229910052719 titanium Inorganic materials 0.000 description 1
- 239000010936 titanium Substances 0.000 description 1
- -1 titanium silicates Chemical class 0.000 description 1
- 239000002351 wastewater Substances 0.000 description 1
- 239000003799 water insoluble solvent Substances 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C29/00—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring
- C07C29/62—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring by introduction of halogen; by substitution of halogen atoms by other halogen atoms
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C29/00—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C31/00—Saturated compounds having hydroxy or O-metal groups bound to acyclic carbon atoms
- C07C31/34—Halogenated alcohols
- C07C31/36—Halogenated alcohols the halogen not being fluorine
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
- Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)
Abstract
Способ высокоселективного каталитического гидрохлорирования глицерина и/или монохлорпропандиолов с получением дихлорпропанольных продуктов - 1,3-дихлор-2-пропанола и 2,3-дихлор-1-пропанола, которые проводят, по крайней мере, в одной непрерывной реакционной зоне при реакционной температуре в пределах 70-140 °С и при постоянном удалении реакционной воды, причем добавленная жидкость содержит, по крайней мере, 50 масс. % глицерина и/или монохлорпропандиолов. Способ можно проводить в непрерывном одностадийном циркуляционном реакторе или каскаде реакторов непрерывного потока жидкостно-газового типа.
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CZ20032346A CZ294890B6 (cs) | 2003-09-01 | 2003-09-01 | Způsob přípravy dichlorpropanolů z glycerinu |
PCT/CZ2004/000049 WO2005021476A1 (en) | 2003-09-01 | 2004-08-23 | Method of preparing dichloropropanols from glycerine |
Publications (1)
Publication Number | Publication Date |
---|---|
UA81971C2 true UA81971C2 (ru) | 2008-02-25 |
Family
ID=34256927
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
UAA200603528A UA81971C2 (ru) | 2003-09-01 | 2004-08-23 | Способ и устройство для получения дихлорпропанолов из глицерина |
Country Status (22)
Country | Link |
---|---|
US (2) | US7473809B2 (ru) |
EP (1) | EP1663924B1 (ru) |
JP (3) | JP5752342B2 (ru) |
KR (1) | KR101062792B1 (ru) |
CN (1) | CN100439305C (ru) |
AT (1) | ATE530513T1 (ru) |
BR (1) | BRPI0413914B1 (ru) |
CA (1) | CA2537131C (ru) |
CY (1) | CY1112165T1 (ru) |
CZ (1) | CZ294890B6 (ru) |
DK (1) | DK1663924T3 (ru) |
ES (1) | ES2373040T3 (ru) |
HK (1) | HK1096081A1 (ru) |
IN (1) | IN2012DN00705A (ru) |
MX (1) | MXPA06002351A (ru) |
PL (1) | PL1663924T3 (ru) |
PT (1) | PT1663924E (ru) |
RU (1) | RU2356878C2 (ru) |
SI (1) | SI1663924T1 (ru) |
TW (1) | TWI325417B (ru) |
UA (1) | UA81971C2 (ru) |
WO (1) | WO2005021476A1 (ru) |
Families Citing this family (68)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CZ294890B6 (cs) * | 2003-09-01 | 2005-04-13 | Spolek Pro Chemickou A Hutní Výrobu,A.S. | Způsob přípravy dichlorpropanolů z glycerinu |
DE602004029724D1 (de) | 2003-11-20 | 2010-12-02 | Solvay | Verfahren zur Herstellung von organischen Verbindungen aus Glycerol, stammend aus nachwachsenden Rohstoffen |
EP1687248B1 (en) | 2003-11-20 | 2011-06-01 | SOLVAY (Société Anonyme) | Process for producing dichloropropanol from glycerol and a chlorinated agent and in the presence of a catalyst selected from adipic and glutaric acid |
US8088957B2 (en) * | 2004-07-21 | 2012-01-03 | Dow Global Technologies Llc | Conversion of a multihydroxylated-aliphatic hydrocarbon or ester thereof to a chlorohydrin |
US7910781B2 (en) | 2004-07-21 | 2011-03-22 | Dow Global Technologies Llc | Process for the conversion of a crude glycerol, crude mixtures of naturally derived multihydroxylated aliphatic hydrocarbons or esters thereof to a chlorohydrin |
US7906690B2 (en) | 2004-07-21 | 2011-03-15 | Dow Global Technologies Inc. | Batch, semi-continuous or continuous hydrochlorination of glycerin with reduced volatile chlorinated hydrocarbon by-products and chloracetone levels |
KR20080037618A (ko) | 2005-05-20 | 2008-04-30 | 솔베이(소시에떼아노님) | 폴리히드록실화 지방족 탄화수소 및 염소화제 간의 반응에의한 클로로히드린 제조 방법 |
EP1885671A1 (fr) * | 2005-05-20 | 2008-02-13 | Solvay SA | Procede de fabrication d'une chlorhydrine au depart d'un hydrocarbure aliphatique poly hydroxyle |
WO2007054505A2 (en) * | 2005-11-08 | 2007-05-18 | Solvay (Société Anonyme) | Process for the manufacture of dichloropropanol by chlorination of glycerol |
EP2043984A1 (en) | 2006-06-14 | 2009-04-08 | Solvay S.A. | Crude glycerol-based product, process for its purification and its use in the manufacture of dichloropropanol |
US7930651B2 (en) | 2007-01-18 | 2011-04-19 | Research In Motion Limited | Agenda display in an electronic device |
FR2913421B1 (fr) | 2007-03-07 | 2009-05-15 | Solvay | Procede de fabrication de dichloropropanol. |
FR2913684B1 (fr) | 2007-03-14 | 2012-09-14 | Solvay | Procede de fabrication de dichloropropanol |
TWI529155B (zh) * | 2007-04-12 | 2016-04-11 | 陶氏全球科技公司 | 用於製造氯醇之方法與裝置 |
US8664453B2 (en) | 2007-04-12 | 2014-03-04 | Dow Global Technologies Inc. | Multi-stage process and apparatus for recovering dichlorohydrins |
KR20100016455A (ko) | 2007-04-12 | 2010-02-12 | 다우 글로벌 테크놀로지스 인크. | 공증류에 의한 다이클로로하이드린 회수 방법 및 장치 |
US20110152580A1 (en) * | 2007-04-12 | 2011-06-23 | Hook Bruce D | Process and apparatus for vapor phase purification during hydrochlorination of multi-hydroxylated aliphatic hydrocarbon compounds |
US8334415B2 (en) | 2007-04-12 | 2012-12-18 | Dow Global Technologies Llc | Process and apparatus for reducing heavy byproduct formation during distillation |
US8629305B2 (en) | 2007-04-12 | 2014-01-14 | Dow Global Technologies Inc | Process and apparatus for azeotropic recovery of dichlorohydrins |
TW200911740A (en) * | 2007-06-01 | 2009-03-16 | Solvay | Process for manufacturing a chlorohydrin |
TW200911693A (en) | 2007-06-12 | 2009-03-16 | Solvay | Aqueous composition containing a salt, manufacturing process and use |
TWI500609B (zh) | 2007-06-12 | 2015-09-21 | Solvay | 含有環氧氯丙烷的產品,其製備及其不同應用中的用途 |
FR2918058A1 (fr) * | 2007-06-28 | 2009-01-02 | Solvay | Produit a base de glycerol, procede pour sa purification et son utilisation dans la fabrication de dichloropropanol |
JP2010241689A (ja) * | 2007-08-17 | 2010-10-28 | Kashima Chemical Kk | クロロヒドリンの製造方法 |
CN101397238B (zh) * | 2007-09-24 | 2011-08-17 | 如皋市双马化工有限公司 | 一种生产二氯丙醇的方法 |
CN101808968B (zh) * | 2007-09-28 | 2013-10-23 | 大曹株式会社 | 氯代醇类的制造方法 |
EP2219779B1 (en) | 2007-11-19 | 2012-05-30 | Conser S.P.A. | Conversion of glycerine to dichlorohydrins and epichlorohydrin |
KR100881344B1 (ko) * | 2007-12-12 | 2009-02-02 | 삼성정밀화학 주식회사 | 헤테로폴리산 촉매를 사용하여 글리세롤로부터디클로로프로판올을 제조하는 방법 |
FR2925045B1 (fr) | 2007-12-17 | 2012-02-24 | Solvay | Produit a base de glycerol, procede pour son obtention et son utilisation dans la fabrication de dichloropropanol |
TWI478875B (zh) | 2008-01-31 | 2015-04-01 | Solvay | 使水性組成物中之有機物質降解之方法 |
DE102008007622A1 (de) | 2008-02-04 | 2009-08-06 | Biopetrol Industries Ag | Verfahren zur Herstellung von Epichlorhydrin aus Glyzerin |
WO2009104961A2 (en) * | 2008-02-21 | 2009-08-27 | Bouwe De Jong | Process for the preparation of a dichloropropanol product |
PL2257537T3 (pl) | 2008-02-26 | 2013-03-29 | Dow Global Technologies Llc | Sposób oczyszczania epichlorohydryn |
AR072446A1 (es) | 2008-03-02 | 2010-09-01 | Dow Global Technologies Inc | Proceso de hidrogenacion mejorado |
CN101980995B (zh) | 2008-04-03 | 2014-06-18 | 索尔维公司 | 包含甘油的组合物、获得该组合物的方法以及它们在二氯丙醇生产中的用途 |
CN101998944B (zh) * | 2008-04-09 | 2014-09-03 | 陶氏环球技术公司 | 用于回收二氯代醇的多级方法和设备 |
BRPI0906911A2 (pt) | 2008-04-09 | 2015-07-21 | Dow Global Technologies Inc | Processo e aparelhagem para recuperar dicloridrinas a partir de uma mistura compreendendo dicloridrinas. |
CN101570470B (zh) * | 2008-04-29 | 2012-08-29 | 中国石油化工股份有限公司 | 一种通过甘油氯化制备二氯丙醇的方法 |
CN101570471B (zh) * | 2008-04-29 | 2012-08-29 | 中国石油化工股份有限公司 | 一种由甘油合成二氯丙醇的方法 |
AT507260B1 (de) * | 2008-08-25 | 2010-10-15 | Kanzler Walter | Verfahren zur herstellung von epichlorhydrin aus glyzerin |
ITMI20081535A1 (it) * | 2008-08-26 | 2010-02-26 | Biocompany Srl | Processo per la preparazione di 1,3-dicloro-2-propanolo |
FR2935968B1 (fr) | 2008-09-12 | 2010-09-10 | Solvay | Procede pour la purification de chlorure d'hydrogene |
CN101429099B (zh) * | 2008-11-25 | 2011-12-07 | 烟台万华聚氨酯股份有限公司 | 一种由甘油制备二氯丙醇的方法 |
KR101067494B1 (ko) * | 2008-12-31 | 2011-09-27 | 삼성정밀화학 주식회사 | 디클로로프로판올의 선택도가 향상된, 글리세롤을 사용하는디클로로프로판올의 제조방법 |
CN101774886B (zh) * | 2009-01-13 | 2013-10-16 | 德纳(南京)化工有限公司 | 二氯丙醇制备方法及反应装置 |
BRPI0901399A2 (pt) * | 2009-03-11 | 2010-11-16 | Ima Quimica S A | processo para obtenção de dicloropropanóis |
WO2011092270A2 (en) | 2010-02-01 | 2011-08-04 | Akzo Nobel Chemicals International B.V. | Process for preparing epichlorohydrin from dichlorohydrin |
KR101705205B1 (ko) * | 2010-06-30 | 2017-02-09 | 롯데정밀화학 주식회사 | 클로로히드린류의 제조방법 및 그 방법에 의해 제조된 클로로히드린류를 사용하는 에피클로로히드린의 제조방법 |
KR101705206B1 (ko) * | 2010-06-30 | 2017-02-09 | 롯데정밀화학 주식회사 | 클로로히드린류의 제조방법 및 그 방법에 의해 제조된 클로로히드린류를 사용하는 에피클로로히드린의 제조방법 |
KR101705208B1 (ko) * | 2010-06-30 | 2017-02-09 | 롯데정밀화학 주식회사 | 클로로히드린류 조성물의 제조방법 및 그 방법에 의해 제조된 클로로히드린류 조성물을 사용하는 에피클로로히드린의 제조방법 |
KR101705210B1 (ko) * | 2010-06-30 | 2017-02-09 | 롯데정밀화학 주식회사 | 클로로히드린류 조성물의 제조방법 및 그 방법에 의해 제조된 클로로히드린류 조성물을 사용하는 에피클로로히드린의 제조방법 |
KR101705207B1 (ko) * | 2010-06-30 | 2017-02-09 | 롯데정밀화학 주식회사 | 클로로히드린류의 제조방법 및 그 방법에 의해 제조된 클로로히드린류를 사용하는 에피클로로히드린의 제조방법 |
KR101705209B1 (ko) * | 2010-06-30 | 2017-02-09 | 롯데정밀화학 주식회사 | 클로로히드린류 조성물의 제조방법 및 그 방법에 의해 제조된 클로로히드린류 조성물을 사용하는 에피클로로히드린의 제조방법 |
RU2575928C2 (ru) | 2010-09-03 | 2016-02-27 | СТЕПАН СПЕШИАЛТИ ПРОДАКТС, ЭлЭлСи | Удаление галогенорганических и оксирановых соединений из потоков сложных эфиров карбоновых кислот |
CN101979365B (zh) * | 2010-09-20 | 2013-11-06 | 华东理工大学 | 一种连续制备二氯丙醇的方法 |
JP6049087B2 (ja) | 2010-09-30 | 2016-12-21 | ソルヴェイ(ソシエテ アノニム) | 天然起源のエピクロロヒドリンの誘導体 |
CN102010295B (zh) * | 2010-11-12 | 2013-05-01 | 珠海长先化学科技有限公司 | 一种甘油法制二氯丙醇的方法 |
PL215730B1 (pl) | 2011-01-10 | 2014-01-31 | Inst Ciezkiej Syntezy Orga | Sposób wytwarzania dichloropropanoli z gliceryny |
PL218074B1 (pl) | 2011-04-11 | 2014-10-31 | Inst Ciężkiej Syntezy Organicznej Blachownia | Sposób suchego chlorowodorowania masy z chlorowodorowania gliceryny kwasem solnym i urządzenie do suchego chlorowodorowania masy z chlorowodorowania gliceryny kwasem solnym |
CN102295529B (zh) * | 2011-07-11 | 2015-09-09 | 江西省化学工业研究所 | 一种用甘油和盐酸连续制备二氯丙醇的方法 |
WO2013034612A1 (en) | 2011-09-09 | 2013-03-14 | Akzo Nobel Chemicals International B.V. | Process for the chlorination of a hydroxylated organic compound |
CZ306363B6 (cs) * | 2013-06-10 | 2016-12-21 | Spolek Pro Chemickou A Hutní Výrobu, Akciová Společnost | Způsob výroby epoxy-monomerů a epoxidů |
CN103570498B (zh) * | 2013-08-06 | 2016-06-22 | 江苏大学 | 一种甘油氯化制备二氯丙醇的方法 |
CN104557442B (zh) * | 2013-10-18 | 2017-10-13 | 江苏扬农化工集团有限公司 | 六氯乙烷的综合利用方法 |
CN104370857A (zh) * | 2014-11-11 | 2015-02-25 | 常州大学 | 一种环氧氯丙烷的合成方法 |
WO2017035403A1 (en) | 2015-08-25 | 2017-03-02 | Dsm Ip Assets B.V. | Refined oil compositions and methods for making |
TWI547470B (zh) * | 2015-12-18 | 2016-09-01 | 長春人造樹脂廠股份有限公司 | 製造二氯丙醇之方法 |
CN111018665A (zh) * | 2019-12-17 | 2020-04-17 | 山东民基化工有限公司 | 环氧氯丙烷重组分中三氯丙烷的回收利用方法 |
Family Cites Families (11)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE197308C (ru) * | ||||
DE1075103B (de) | 1960-02-11 | VEB Leuna-Werke "Walter Ulbricht", Leuna (Kr. Merseburg) | Verfahren zur kontinuierlichen Herstellung von Epichlorhydrin aus Glyzerin | |
US2144612A (en) * | 1936-09-10 | 1939-01-24 | Dow Chemical Co | Preparation of glycerol dichlorohydrin |
US2198600A (en) | 1936-09-10 | 1940-04-30 | Dow Chemical Co | Glycerol dichlorohydrin |
JPH0643353B2 (ja) * | 1989-07-25 | 1994-06-08 | ダイソー株式会社 | 2,3―ジクロロ―1―プロパノールの連続的製法及びその装置 |
JP3846926B2 (ja) | 1995-12-27 | 2006-11-15 | 日本ジーイープラスチックス株式会社 | 芳香族カーボネートの連続的製造方法 |
DE19604253A1 (de) * | 1996-02-06 | 1997-08-07 | Basf Ag | Verfahren zur kontinuierlichen Herstellung von Alkylestern der (Meth)acrylsäure |
JP2002020333A (ja) * | 2000-07-06 | 2002-01-23 | Toagosei Co Ltd | 水酸基の塩素化方法 |
DE10063175A1 (de) * | 2000-12-18 | 2002-06-20 | Basf Ag | Verfahren zur Herstellung von höheren (Meth)acrylsäureestern |
JP4721311B2 (ja) * | 2001-04-26 | 2011-07-13 | 昭和電工株式会社 | 2,3−ジクロル−1−プロパノール及びエピクロルヒドリンの製造方法 |
CZ294890B6 (cs) | 2003-09-01 | 2005-04-13 | Spolek Pro Chemickou A Hutní Výrobu,A.S. | Způsob přípravy dichlorpropanolů z glycerinu |
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