JPWO2018134239A5 - - Google Patents
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- JPWO2018134239A5 JPWO2018134239A5 JP2019538621A JP2019538621A JPWO2018134239A5 JP WO2018134239 A5 JPWO2018134239 A5 JP WO2018134239A5 JP 2019538621 A JP2019538621 A JP 2019538621A JP 2019538621 A JP2019538621 A JP 2019538621A JP WO2018134239 A5 JPWO2018134239 A5 JP WO2018134239A5
- Authority
- JP
- Japan
- Prior art keywords
- station
- hydrochloric acid
- supplied
- hcl
- pick
- 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.)
- Pending
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- VEXZGXHMUGYJMC-UHFFFAOYSA-N HCl Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 14
- 229910000041 hydrogen chloride Inorganic materials 0.000 description 4
- IXCSERBJSXMMFS-UHFFFAOYSA-N hydrogen chloride Substances Cl.Cl IXCSERBJSXMMFS-UHFFFAOYSA-N 0.000 description 4
- 238000005868 electrolysis reaction Methods 0.000 description 3
- HEMHJVSKTPXQMS-UHFFFAOYSA-M sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 3
- 230000005591 charge neutralization Effects 0.000 description 2
- 230000001264 neutralization Effects 0.000 description 2
- 238000006386 neutralization reaction Methods 0.000 description 2
- 238000010521 absorption reaction Methods 0.000 description 1
- 150000008044 alkali metal hydroxides Chemical class 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000012266 salt solution Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 238000004642 transportation engineering Methods 0.000 description 1
Description
本発明は、連続した化学品製造プロセスから得られる、少なくとも10重量%のHCl濃度を有する、特に少なくとも1m3/hの体積流量での塩酸の使用を柔軟に制御するための方法を提供し、精製された塩酸は、選択的に、塩酸の引き取り場所である塩酸貯蔵所、輸送ステーション、HCl電解ステーションまたはクロルアルカリ電解ステーションに供給され、または中和ステーションに供給され、1つまたは複数の上述の引き取り場所が故障した場合、または引き取り場所での引き取り障害の場合に、塩酸は中和ステーションに供給され、濃アルカリ金属水酸化物、特に濃水酸化ナトリウムで中和され、そして形成された塩溶液は、選択的にクロルアルカリ電解ステーションまたは廃棄ステーションに供給される。 The present invention provides a method for flexibly controlling the use of hydrochloric acid, which is obtained from a continuous chemical manufacturing process and has a HCl concentration of at least 10% by weight, particularly at a volumetric flow rate of at least 1 m3 / h. The hydrochloric acid that has been prepared is selectively supplied to a hydrochloric acid storage, a transportation station, an HCl electrolysis station or a chloralkali electrolysis station, which is a collection place of hydrochloric acid, or is supplied to a neutralization station , and one or more of the above-mentioned collections described above. In the event of a site failure, or a pick-up failure at the pick-up location, hydrochloric acid is supplied to the neutralization station, neutralized with concentrated alkali metal hydroxides, especially concentrated sodium hydroxide, and the salt solution formed. , Optionally supplied to the chloralkali electrolysis station or disposal station.
代替的に、塩化水素吸収のためにHClガス流41をステーションCに直接供給することもできる。 Alternatively, an HCl gas stream 41 can be supplied directly to station C for hydrogen chloride absorption.
Applications Claiming Priority (3)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
EP17152417.6A EP3351505A1 (en) | 2017-01-20 | 2017-01-20 | Method for flexible control of the use of hydrochloric acid from chemical production |
EP17152417.6 | 2017-01-20 | ||
PCT/EP2018/051088 WO2018134239A1 (en) | 2017-01-20 | 2018-01-17 | Method for flexibly controlling the use of hydrochloric acid from chemical production |
Publications (2)
Publication Number | Publication Date |
---|---|
JP2020506859A JP2020506859A (en) | 2020-03-05 |
JPWO2018134239A5 true JPWO2018134239A5 (en) | 2022-05-16 |
Family
ID=58017897
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP2019538621A Pending JP2020506859A (en) | 2017-01-20 | 2018-01-17 | A flexible way to control the use of hydrochloric acid from chemical manufacturing |
Country Status (6)
Country | Link |
---|---|
US (1) | US11040878B2 (en) |
EP (2) | EP3351505A1 (en) |
JP (1) | JP2020506859A (en) |
KR (1) | KR20190105590A (en) |
CN (1) | CN110198914A (en) |
WO (1) | WO2018134239A1 (en) |
Families Citing this family (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN109399567B (en) * | 2018-12-28 | 2021-08-13 | 甘肃金川恒信高分子科技有限公司 | Automatic compensation hydrogen chloride generator |
BR102020009844A2 (en) * | 2020-05-15 | 2021-11-23 | Petróleo Brasileiro S.A. - Petrobras | METHOD AND APPARATUS FOR EVALUATION OF THE EVOLUTION OF HYDROGEN CHLORIDE AS A FUNCTION OF TEMPERATURE |
Family Cites Families (28)
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AT234639B (en) * | 1961-10-14 | 1964-07-10 | Siegener Ag Eisenkonstruktion | Process for the production of gaseous chlorine and gaseous hydrogen |
JPS5311238B2 (en) * | 1972-09-14 | 1978-04-20 | ||
US4247532A (en) * | 1979-08-13 | 1981-01-27 | Shell Oil Company | Purification of electrolytically-produced chlorine |
DE3714439A1 (en) | 1987-04-30 | 1988-11-10 | Bayer Ag | METHOD FOR PRODUCING (CYCLO) ALIPHATIC DIISOCYANATES |
EP0371201A1 (en) * | 1988-12-01 | 1990-06-06 | Ruhrkohle Aktiengesellschaft | Process for the hydrogenation of chloroorganic compounds and neutralisation of the resulting hydrogen chloride, and neutralising agent for hydrogen chloride resulting from chloroorganic compounds |
FI85007C (en) * | 1990-10-24 | 1992-02-25 | Nokia Ab Chemicals Oy | Process for the production of hydrochloric acid |
US5616234A (en) * | 1995-10-31 | 1997-04-01 | Pepcon Systems, Inc. | Method for producing chlorine or hypochlorite product |
IT1282367B1 (en) * | 1996-01-19 | 1998-03-20 | De Nora Spa | IMPROVED METHOD FOR THE ELECTROLYSIS OF WATER SOLUTIONS OF HYDROCHLORIC ACID |
JPH1081986A (en) * | 1996-09-03 | 1998-03-31 | Permelec Electrode Ltd | Horizontal double-polarity electrolytic cell |
US6719957B2 (en) | 2002-04-17 | 2004-04-13 | Bayer Corporation | Process for purification of anhydrous hydrogen chloride gas |
US20040152929A1 (en) * | 2002-05-08 | 2004-08-05 | Clarke William D | Process for vinyl chloride manufacture from ethane and ethylene with air feed and alternative hcl processing methods |
DE102005032663A1 (en) | 2005-07-13 | 2007-01-18 | Bayer Materialscience Ag | Process for the preparation of isocyanates |
DE102006023581A1 (en) * | 2006-05-19 | 2007-11-22 | Bayer Materialscience Ag | Process for separating chlorine from the product gas of an HCl oxidation process |
DE102006024516A1 (en) * | 2006-05-23 | 2007-11-29 | Bayer Materialscience Ag | Process for the production of chlorine from hydrogen chloride and oxygen |
CN101583591B (en) | 2007-01-08 | 2014-01-08 | 巴斯夫欧洲公司 | Method for the production of diphenylmethane diamine |
MX346694B (en) * | 2007-04-12 | 2017-03-29 | Cefco Llc * | Process and apparatus for carbon capture and elimination of multi-pollutants in flue gas from hydrocarbon fuel sources and recovery of multiple by-products. |
TWI478875B (en) * | 2008-01-31 | 2015-04-01 | Solvay | Process for degrading organic substances in an aqueous composition |
CA2715874C (en) * | 2008-02-19 | 2019-06-25 | Global Research Technologies, Llc | Extraction and sequestration of carbon dioxide |
DE102008012037A1 (en) * | 2008-03-01 | 2009-09-03 | Bayer Materialscience Ag | Process for the preparation of methylene diphenyl diisocyanates |
DE102008015901A1 (en) * | 2008-03-27 | 2009-10-01 | Bayer Technology Services Gmbh | Electrolysis cell for hydrogen chloride electrolysis |
JP5484689B2 (en) * | 2008-04-25 | 2014-05-07 | 三菱重工業株式会社 | Exhaust gas treatment system and method for removing mercury in exhaust gas |
JP5391577B2 (en) * | 2008-05-14 | 2014-01-15 | Jfeスチール株式会社 | Hydrochloric acid recovery device and hydrochloric acid recovery method for recovering hydrochloric acid from waste hydrochloric acid solution |
US20110091366A1 (en) * | 2008-12-24 | 2011-04-21 | Treavor Kendall | Neutralization of acid and production of carbonate-containing compositions |
ES2643234T3 (en) | 2010-03-30 | 2017-11-21 | Covestro Deutschland Ag | Procedure for the preparation of diaryl carbonates and polycarbonates |
CN102602892B (en) * | 2012-04-11 | 2015-04-01 | 万华化学集团股份有限公司 | Method for preparing chlorine gas through catalytic oxidation of hydrogen chloride |
US20170107128A1 (en) * | 2012-09-07 | 2017-04-20 | Clean Chemistry, Inc. | System and method for generation of reactive oxygen species and applications thereof |
CN104512865B (en) * | 2013-09-26 | 2016-08-17 | 宝山钢铁股份有限公司 | Except in silicon and reaction neutralize medicament ammonia addition control method |
US10934627B2 (en) * | 2016-05-06 | 2021-03-02 | Malvi Technologies, Llc | Methods and systems for making hypochlorite solution from reverse osmosis brine |
-
2017
- 2017-01-20 EP EP17152417.6A patent/EP3351505A1/en not_active Withdrawn
-
2018
- 2018-01-17 CN CN201880007462.2A patent/CN110198914A/en active Pending
- 2018-01-17 EP EP18700374.4A patent/EP3571157A1/en not_active Ceased
- 2018-01-17 JP JP2019538621A patent/JP2020506859A/en active Pending
- 2018-01-17 KR KR1020197020805A patent/KR20190105590A/en not_active Application Discontinuation
- 2018-01-17 WO PCT/EP2018/051088 patent/WO2018134239A1/en unknown
- 2018-01-17 US US16/479,083 patent/US11040878B2/en active Active
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