CS251464B1 - Glass tube reactor for sodium hypochlorite production - Google Patents
Glass tube reactor for sodium hypochlorite production Download PDFInfo
- Publication number
- CS251464B1 CS251464B1 CS84234A CS23484A CS251464B1 CS 251464 B1 CS251464 B1 CS 251464B1 CS 84234 A CS84234 A CS 84234A CS 23484 A CS23484 A CS 23484A CS 251464 B1 CS251464 B1 CS 251464B1
- Authority
- CS
- Czechoslovakia
- Prior art keywords
- sodium hypochlorite
- glass tube
- glass
- production
- tube reactor
- Prior art date
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- 239000011521 glass Substances 0.000 title claims abstract description 17
- 238000004519 manufacturing process Methods 0.000 title claims abstract description 9
- 239000005708 Sodium hypochlorite Substances 0.000 title abstract description 9
- SUKJFIGYRHOWBL-UHFFFAOYSA-N sodium hypochlorite Chemical compound [Na+].Cl[O-] SUKJFIGYRHOWBL-UHFFFAOYSA-N 0.000 title abstract description 9
- 239000012071 phase Substances 0.000 claims abstract description 8
- 239000007791 liquid phase Substances 0.000 claims abstract description 6
- ZAMOUSCENKQFHK-UHFFFAOYSA-N Chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 claims description 2
- 239000000460 chlorine Substances 0.000 claims description 2
- 229910052801 chlorine Inorganic materials 0.000 claims description 2
- -1 sodium propyne Chemical compound 0.000 claims 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims 1
- 238000006243 chemical reaction Methods 0.000 description 7
- 229910000831 Steel Inorganic materials 0.000 description 1
- 239000004809 Teflon Substances 0.000 description 1
- 229920006362 Teflon® Polymers 0.000 description 1
- RTAQQCXQSZGOHL-UHFFFAOYSA-N Titanium Chemical compound [Ti] RTAQQCXQSZGOHL-UHFFFAOYSA-N 0.000 description 1
- 239000002826 coolant Substances 0.000 description 1
- 239000012467 final product Substances 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 230000007246 mechanism Effects 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 229910052573 porcelain Inorganic materials 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 239000011541 reaction mixture Substances 0.000 description 1
- 238000007789 sealing Methods 0.000 description 1
- 239000010959 steel Substances 0.000 description 1
- 229910052719 titanium Inorganic materials 0.000 description 1
- 239000010936 titanium Substances 0.000 description 1
Landscapes
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Abstract
Riešenie sa týká skleněného rúrkového reaktora na výrobu chlórnanu sodného, ktorý pozostáva z horizontálně uložených skleněných rúrok sériovo alebo sériovo-paralelne vzájomne přepojených, opatřených prívodom kvapalnej fázy, prívodom plynnej fázy a v spodnej časti vyprázdňovacim otvorom.The solution relates to glass tubular a reactor for the production of sodium hypochlorite, which consists of horizontally mounted glass pipes in series or in series interconnected, provided with inlet of the liquid phase by supplying the gas phase and, at the bottom, a discharge opening.
Description
Vynález sa týká skleněného rúrkového reaktora na výrobu chlornanu sodného.The present invention relates to a glass tubular reactor for the production of sodium hypochlorite.
Je známe, že na výrobu chlornanu sodného v prostředí reakčného procesu je vhodné zariadenie z úzkoprofilového a cenove vel'mi nákladného materiálu-titanu. Čiastočne vyhovuje pri technologickom procese pogumované, respektive porcelánové zariadenie. Obe tieto zariadenia majú obmedzenú životnost, sú poruchové a nevýkonné. Používá sa aj zariadenie vyhotovené z vertikálně vedl'a sebe umiestnených skleněných rúr, ktoré sú uchytené komplikovaným teflonovým těsněním v ocelovom, zo strany reakčného procesu pogumovanom plášti. Toto zariadenie nezaručuje kontakt zložiek pri reakcii, dosledkom čoho plynná fáza može niektorými rúrkami unikat nekontrolovatelné, čím vznikajú straty na surovinách. Toto zariadenie vzhladom na nadobúdaciu hodnotu a dosahovaný výkon je neúmerne nákladné a je značné poruchové.It is known that a device made of low-profile and costly titanium material is suitable for the production of sodium hypochlorite in the reaction process environment. Particularly suitable for the technological process is rubber or porcelain equipment. Both of these devices have a limited lifetime, are faulty and inefficient. Also used is a device made of vertically adjacent glass tubes, which are attached by a complicated teflon seal in a steel-coated rubberized jacket. This device does not guarantee the contact of the components during the reaction, as a result of which the gas phase may escape uncontrolled through some tubes, resulting in loss of raw materials. This device is disproportionately costly and failing due to the acquisition value and the power achieved.
Uvedené nedostatky odstraňuje skleněný rúrkový reaktor na výrobu chlornanu sodného podlá vynálezu, ktorého podstata spočívá v tom, že pozostáva z horizontálně uložených skleněných rúrok sériovo alebo sériovo-paralelne vzájomne přepojených, opatřených prívodom kvapalnej fázy, prívodom plynnej fázy a v spodnej časti vyprázdňovacírn otvorom.The above-mentioned drawbacks are overcome by the glass tubular reactor for the production of sodium hypochlorite according to the invention, which consists of horizontally arranged glass tubes connected in series or in parallel to each other, provided with a liquid phase inlet, a gas phase inlet and a discharge opening at the bottom.
Výhoda skleněného rúrkového reaktora na výrobu chlornanu sodného spočívá predovšetkým v možnosti využitia sériovo vyrábaných skleněných rúrok, tvaroviek a spojovacieho tesnenia, čím sa podstatné znižujú investičně náklady — až o 50 % pri dosahovaní rovnakého produkčného výkonu v porovnaní s vertikálně umiestnenými skleněnými rúrami.The advantage of a glass tubular reactor for the production of sodium hypochlorite lies primarily in the possibility of using mass-produced glass tubes, fittings and joint gaskets, thereby significantly reducing investment costs - up to 50% while achieving the same production performance compared to vertically placed glass tubes.
Jednoduchá konštrukcia skleněného rúrkového reaktora umožňuje skonštruovať reaktor na akúkolvek požadovanú hodlnovú kapacitu výroby chlórnanu sodného v jednom uzatvorenom systéme.The simple design of the glass tubular reactor allows the reactor to be constructed to any desired capacity for producing sodium hypochlorite in a single closed system.
Dalšou přednostou skleněného rúrkového reaktora podlá vynálezu je, že ku všetkým tesniacim spojom je 1'ahký montážny přístup. Jednotlivé rúrky sú l'ahko demontovatelné a je ich možné vymieňať bez použitia mechanizmov, čo má pozitivny význam pre údržbu zariadenia. Reakčný proces v tomto reaktore je možné vizuálně sledovat. Je zaručený kontakt kvapalnej a plynnej fázy; prostredie pri reakčnom procese je dokonale čisté.Another advantage of the glass tube reactor according to the invention is that all sealing joints are easy to assemble. The individual tubes are easily removable and can be replaced without the use of mechanisms, which is of positive importance for the maintenance of the equipment. The reaction process in this reactor can be visually monitored. Liquid and gaseous contact is guaranteed; the environment in the reaction process is perfectly clean.
Skleněný rúrkový reaktor na výrobu chlórnanu sodného je znázorněný na priloženom obrázku. Pozostáva zo skleněných rúrok 1, ktoré sú uložené horizontálně a sú sériovo alebo sériovo-paralelne vzájomne přepojené, opatřené sú prívodom 2 kvapalnej fázy, prívodom 3 plynnej fázy, bočným vstupom 6 pro přívod chlóru a v spodnej časti vyprázdňovacím otvorom.A glass tubular reactor for producing sodium hypochlorite is shown in the attached figure. It consists of glass tubes 1 which are arranged horizontally and are connected in series or series-parallel interconnections, provided with a liquid phase inlet 2, a gas phase inlet 3, a chlorine inlet side inlet 6 and a discharge opening at the bottom.
Kvapalná fáza sa privádza do skleněného rúrkového reaktora prívodom 2 kvapalnej fázy (potrubím) zo zásobníka 7 pomocou čerpadla 8, podobné sa privádza prívodom 3 plynnej fázy plynná zložka. Teplo, vznikajúce exotermickou reakciou, sa odvádza chladiacim médiom 4. Plynná fáza sa po reakcii odsává ventilátorom 5. Reakčná zmes sa zo skleněného rúrkového reaktora odvádza vyprázdňovacím otvorom do zásobníkaThe liquid phase is supplied to the glass tube reactor by supplying 2 of the liquid phase (via a line) from the reservoir 7 by means of a pump 8, similarly the gas component is supplied by supplying the gas phase 3. The heat generated by the exothermic reaction is removed by the cooling medium 4. The gas phase is sucked off by the fan 5 after the reaction. The reaction mixture is discharged from the glass tube reactor through a discharge opening to a storage tank.
7.7th
Pri takomto usporiadaní produkČnej stanice na výrobu chlórnanu sodného sa dosahuje hodinový výkon vztiahnutý na objem média v rúrkach reaktora až 150 kg finálneho produktu na 100 litrov reakčného objemu.With such a configuration of the sodium hypochlorite production station, an hourly output, based on the volume of the medium in the reactor tubes, achieves up to 150 kg of final product per 100 liters of reaction volume.
Claims (1)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CS84234A CS251464B1 (en) | 1984-01-11 | 1984-01-11 | Glass tube reactor for sodium hypochlorite production |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CS84234A CS251464B1 (en) | 1984-01-11 | 1984-01-11 | Glass tube reactor for sodium hypochlorite production |
Publications (2)
Publication Number | Publication Date |
---|---|
CS23484A1 CS23484A1 (en) | 1986-11-13 |
CS251464B1 true CS251464B1 (en) | 1987-07-16 |
Family
ID=5334109
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CS84234A CS251464B1 (en) | 1984-01-11 | 1984-01-11 | Glass tube reactor for sodium hypochlorite production |
Country Status (1)
Country | Link |
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CS (1) | CS251464B1 (en) |
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1984
- 1984-01-11 CS CS84234A patent/CS251464B1/en unknown
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Publication number | Publication date |
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CS23484A1 (en) | 1986-11-13 |
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