MX2017012236A - Metodo para recuperar hcl de una corriente gaseosa que contiene hcl. - Google Patents

Metodo para recuperar hcl de una corriente gaseosa que contiene hcl.

Info

Publication number
MX2017012236A
MX2017012236A MX2017012236A MX2017012236A MX2017012236A MX 2017012236 A MX2017012236 A MX 2017012236A MX 2017012236 A MX2017012236 A MX 2017012236A MX 2017012236 A MX2017012236 A MX 2017012236A MX 2017012236 A MX2017012236 A MX 2017012236A
Authority
MX
Mexico
Prior art keywords
hcl
gas stream
containing gas
dca
mca
Prior art date
Application number
MX2017012236A
Other languages
English (en)
Inventor
Kooijman Cornelis
Jan Vos Hendrik
Magnus Tollin Lars
Original Assignee
Akzo Nobel Chemicals Int Bv
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 Akzo Nobel Chemicals Int Bv filed Critical Akzo Nobel Chemicals Int Bv
Publication of MX2017012236A publication Critical patent/MX2017012236A/es

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D53/00Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/14Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by absorption
    • B01D53/1406Multiple stage absorption
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D53/00Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/14Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by absorption
    • B01D53/1456Removing acid components
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D53/00Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/14Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by absorption
    • B01D53/1493Selection of liquid materials for use as absorbents
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D53/00Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/34Chemical or biological purification of waste gases
    • B01D53/46Removing components of defined structure
    • B01D53/68Halogens or halogen compounds
    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01BNON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B7/00Halogens; Halogen acids
    • C01B7/01Chlorine; Hydrogen chloride
    • C01B7/07Purification ; Separation
    • C01B7/0706Purification ; Separation of hydrogen chloride
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C51/00Preparation of carboxylic acids or their salts, halides or anhydrides
    • C07C51/347Preparation of carboxylic acids or their salts, halides or anhydrides by reactions not involving formation of carboxyl groups
    • C07C51/377Preparation of carboxylic acids or their salts, halides or anhydrides by reactions not involving formation of carboxyl groups by splitting-off hydrogen or functional groups; by hydrogenolysis of functional groups
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C51/00Preparation of carboxylic acids or their salts, halides or anhydrides
    • C07C51/42Separation; Purification; Stabilisation; Use of additives
    • C07C51/487Separation; Purification; Stabilisation; Use of additives by treatment giving rise to chemical modification
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D2252/00Absorbents, i.e. solvents and liquid materials for gas absorption
    • B01D2252/10Inorganic absorbents
    • B01D2252/103Water
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D2257/00Components to be removed
    • B01D2257/20Halogens or halogen compounds
    • B01D2257/204Inorganic halogen compounds
    • B01D2257/2045Hydrochloric acid

Abstract

La invención se refiere a un método para recuperar HCI de una corriente gaseosa que contiene HCI en donde se suministra una corriente gaseosa que contiene HCI con una temperatura de -20 a 25°C a una unidad de absorción adiabática en donde se pone en contacto con agua como absorbente, resultando en la formación de una corriente gaseosa superior y una solución acuosa de producto HCI, en donde la temperatura de la corriente gaseosa superior es al menos 70°C y en donde la solución acuosa de producto HCI tiene una concentración de HCI en el rango de 5-20% en peso. Se prefiere que la corriente gaseosa que contiene HCI derive de un paso de hidrogenación en donde se hace reaccionar una alimentación que comprende ácido monocloroacético (MCA) y ácido dicloroacético (DCA) con hidrógeno para formar una corriente gaseosa que contiene HCI y una corriente de producto que comprende MCA y una cantidad reducida de DCA. La solución de producto HCI se diluye preferiblemente hasta una concentración de 1-8% en peso y la solución diluida se utiliza como absorbente en un segundo paso de absorción, en donde se absorbe HCI de una corriente gaseosa adicional que contiene HCI para formar una segunda solución acuosa de HCI. La corriente gaseosa adicional que contiene HCI deriva preferiblemente de un paso de cloración en donde se hace reaccionar ácido acético con cloro, resultando en la formación de la corriente gaseosa adicional que contiene HCI y una alimentación que comprende ácido monocloroacético (MCA) y ácido dicloroacético (DCA).
MX2017012236A 2015-03-30 2016-03-25 Metodo para recuperar hcl de una corriente gaseosa que contiene hcl. MX2017012236A (es)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
EP15161666 2015-03-30
PCT/EP2016/056688 WO2016156257A1 (en) 2015-03-30 2016-03-25 METHOD FOR RECOVERING HCl FROM A HCl CONTAINING GAS STREAM

Publications (1)

Publication Number Publication Date
MX2017012236A true MX2017012236A (es) 2018-01-23

Family

ID=52875516

Family Applications (1)

Application Number Title Priority Date Filing Date
MX2017012236A MX2017012236A (es) 2015-03-30 2016-03-25 Metodo para recuperar hcl de una corriente gaseosa que contiene hcl.

Country Status (14)

Country Link
US (1) US10773957B2 (es)
EP (1) EP3277625B1 (es)
JP (1) JP6655098B2 (es)
CN (2) CN113772629A (es)
AR (1) AR104109A1 (es)
AU (1) AU2016240368B2 (es)
BR (1) BR112017019363B1 (es)
CO (1) CO2017008839A2 (es)
MX (1) MX2017012236A (es)
PL (1) PL3277625T3 (es)
RU (1) RU2710335C2 (es)
SA (1) SA517382303B1 (es)
WO (1) WO2016156257A1 (es)
ZA (1) ZA201706097B (es)

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP3589205B1 (en) * 2017-03-01 2021-02-03 Fenwal, Inc. Sample tube holder and system
US11446612B2 (en) 2019-08-14 2022-09-20 King Fahd University Of Petroleum And Minerals Simultaneous sorption of dyes and toxic metals from waters using titania-incorporated polyamide
CN111268647B (zh) * 2020-04-15 2021-03-16 浙江博瑞电子科技有限公司 一种HCl中不饱和含氟有机杂质的脱除方法

Family Cites Families (18)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR1313784A (fr) * 1960-09-20 1963-01-04 Hoechst Ag Procédé et installation de réglage pour concentrer des solutions d'acide chlorhydrique obtenues à partir de gaz chlorhydriques
BE631236A (es) * 1962-04-19
JPS5236999B1 (es) * 1966-08-17 1977-09-19
US3658483A (en) * 1970-05-18 1972-04-25 Sued Chemie Ag Apparatus for the production of concentrated hydrohalogen acids and metal oxides
IT951600B (it) * 1971-11-17 1973-07-10 Sir Soc Italiana Resine Spa Miglioramenti relativi alla prepa razione di soluzioni acquose di acido cloridrico
DE2522286C3 (de) 1975-05-20 1978-05-18 Hoechst Ag, 6000 Frankfurt Verfahren zur Reinigung von Rohchlorwasserstoff
JPS5236999A (en) 1975-09-18 1977-03-22 Omron Tateisi Electronics Co Traffic signal control unit
US4488884A (en) * 1983-10-19 1984-12-18 Mobay Chemical Corporation Process for the production of aqueous hydrochloric acid having a concentration of at least 35.5% by weight
DE3526801A1 (de) * 1985-07-26 1987-02-05 Hoechst Ag Verfahren zur reinigung von chlorwasserstoffgas
JPH0742085B2 (ja) 1986-08-20 1995-05-10 ダイセル化学工業株式会社 塩化水素ガスの精製方法
PL167441B1 (pl) 1991-04-05 1995-09-30 Politechnika Szczecinska Sposób wytwarzania kwasu solnego o żądanym stężeniu pozbawionego zanieczyszczeń chloroorganicznych i dwutlenku siarki
EP0618170B1 (en) * 1993-03-31 1996-09-04 Basf Corporation Process for producing reagent grade hydrochloric acid from the manufacture of organic isocyanates
EP1900719A1 (en) 2006-09-01 2008-03-19 BUSS ChemTech AG Manufacture of substantially pure monochloroacetic acid
CN101190396A (zh) 2006-11-28 2008-06-04 张天德 一种氯乙酸尾气净化及综合利用方法
CN101823694B (zh) 2010-05-06 2012-04-25 杭州四面体科技有限公司 一种含硫的氯化氢净化处理方法
CN102249189A (zh) 2011-05-27 2011-11-23 许昌东方化工有限公司 氯乙酸生产中盐酸的回收方法
MX347055B (es) * 2011-10-20 2017-04-10 Akzo Nobel Chemicals Int Bv Proceso para la purificacion de una alimentacion liquida que comprende mca y dca.
CN104258690B (zh) * 2014-09-22 2018-04-10 中国天辰工程有限公司 氯乙酸生产过程中盐酸尾气吸收制取副产品盐酸的方法

Also Published As

Publication number Publication date
BR112017019363B1 (pt) 2022-08-30
CN113772629A (zh) 2021-12-10
JP6655098B2 (ja) 2020-02-26
BR112017019363A2 (pt) 2018-06-05
EP3277625B1 (en) 2021-05-05
RU2017134720A (ru) 2019-04-04
US20180057358A1 (en) 2018-03-01
PL3277625T3 (pl) 2021-11-02
RU2017134720A3 (es) 2019-08-16
AU2016240368A1 (en) 2017-09-07
ZA201706097B (en) 2019-08-28
AU2016240368B2 (en) 2020-03-05
EP3277625A1 (en) 2018-02-07
WO2016156257A1 (en) 2016-10-06
SA517382303B1 (ar) 2021-09-08
CN106536405A (zh) 2017-03-22
CO2017008839A2 (es) 2017-08-31
JP2018513090A (ja) 2018-05-24
RU2710335C2 (ru) 2019-12-25
US10773957B2 (en) 2020-09-15
AR104109A1 (es) 2017-06-28

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