CH97595A - Process for purifying acetylene. - Google Patents
Process for purifying acetylene.Info
- Publication number
- CH97595A CH97595A CH97595DA CH97595A CH 97595 A CH97595 A CH 97595A CH 97595D A CH97595D A CH 97595DA CH 97595 A CH97595 A CH 97595A
- Authority
- CH
- Switzerland
- Prior art keywords
- acetylene
- solution
- chlorine
- free
- acid
- Prior art date
Links
- HSFWRNGVRCDJHI-UHFFFAOYSA-N alpha-acetylene Natural products C#C HSFWRNGVRCDJHI-UHFFFAOYSA-N 0.000 title claims description 11
- 125000002534 ethynyl group Chemical group [H]C#C* 0.000 title claims description 11
- 238000000034 method Methods 0.000 title claims description 7
- WQYVRQLZKVEZGA-UHFFFAOYSA-N hypochlorite Chemical compound Cl[O-] WQYVRQLZKVEZGA-UHFFFAOYSA-N 0.000 claims description 13
- QWPPOHNGKGFGJK-UHFFFAOYSA-N hypochlorous acid Chemical compound ClO QWPPOHNGKGFGJK-UHFFFAOYSA-N 0.000 claims description 6
- 239000002253 acid Substances 0.000 claims description 5
- BVKZGUZCCUSVTD-UHFFFAOYSA-M Bicarbonate Chemical compound OC([O-])=O BVKZGUZCCUSVTD-UHFFFAOYSA-M 0.000 claims description 4
- 239000003513 alkali Substances 0.000 claims description 4
- 150000003839 salts Chemical class 0.000 claims description 3
- QLOKJRIVRGCVIM-UHFFFAOYSA-N 1-[(4-methylsulfanylphenyl)methyl]piperazine Chemical compound C1=CC(SC)=CC=C1CN1CCNCC1 QLOKJRIVRGCVIM-UHFFFAOYSA-N 0.000 claims description 2
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 2
- 230000015572 biosynthetic process Effects 0.000 claims description 2
- 229910002804 graphite Inorganic materials 0.000 claims description 2
- 239000010439 graphite Substances 0.000 claims description 2
- 238000000746 purification Methods 0.000 claims description 2
- ZAMOUSCENKQFHK-UHFFFAOYSA-N Chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 description 9
- 239000000460 chlorine Substances 0.000 description 9
- 229910052801 chlorine Inorganic materials 0.000 description 9
- 239000007789 gas Substances 0.000 description 5
- 238000004140 cleaning Methods 0.000 description 4
- 238000004880 explosion Methods 0.000 description 4
- XYFCBTPGUUZFHI-UHFFFAOYSA-N Phosphine Chemical compound P XYFCBTPGUUZFHI-UHFFFAOYSA-N 0.000 description 3
- 239000012535 impurity Substances 0.000 description 3
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 2
- UIIMBOGNXHQVGW-UHFFFAOYSA-M Sodium bicarbonate Chemical compound [Na+].OC([O-])=O UIIMBOGNXHQVGW-UHFFFAOYSA-M 0.000 description 2
- 239000000654 additive Substances 0.000 description 2
- 235000011007 phosphoric acid Nutrition 0.000 description 2
- 150000003016 phosphoric acids Chemical class 0.000 description 2
- WKBOTKDWSSQWDR-UHFFFAOYSA-N Bromine atom Chemical compound [Br] WKBOTKDWSSQWDR-UHFFFAOYSA-N 0.000 description 1
- BVKZGUZCCUSVTD-UHFFFAOYSA-L Carbonate Chemical compound [O-]C([O-])=O BVKZGUZCCUSVTD-UHFFFAOYSA-L 0.000 description 1
- RWSOTUBLDIXVET-UHFFFAOYSA-N Dihydrogen sulfide Chemical compound S RWSOTUBLDIXVET-UHFFFAOYSA-N 0.000 description 1
- 239000005708 Sodium hypochlorite Substances 0.000 description 1
- 125000000218 acetic acid group Chemical group C(C)(=O)* 0.000 description 1
- 230000002378 acidificating effect Effects 0.000 description 1
- 150000007513 acids Chemical class 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- GDTBXPJZTBHREO-UHFFFAOYSA-N bromine Substances BrBr GDTBXPJZTBHREO-UHFFFAOYSA-N 0.000 description 1
- 229910052794 bromium Inorganic materials 0.000 description 1
- 239000001569 carbon dioxide Substances 0.000 description 1
- 229910002092 carbon dioxide Inorganic materials 0.000 description 1
- BVKZGUZCCUSVTD-UHFFFAOYSA-N carbonic acid Chemical compound OC(O)=O BVKZGUZCCUSVTD-UHFFFAOYSA-N 0.000 description 1
- 125000005588 carbonic acid salt group Chemical group 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- KRVSOGSZCMJSLX-UHFFFAOYSA-L chromic acid Substances O[Cr](O)(=O)=O KRVSOGSZCMJSLX-UHFFFAOYSA-L 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000005868 electrolysis reaction Methods 0.000 description 1
- 239000003792 electrolyte Substances 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- AWJWCTOOIBYHON-UHFFFAOYSA-N furo[3,4-b]pyrazine-5,7-dione Chemical compound C1=CN=C2C(=O)OC(=O)C2=N1 AWJWCTOOIBYHON-UHFFFAOYSA-N 0.000 description 1
- 229910000037 hydrogen sulfide Inorganic materials 0.000 description 1
- 230000002401 inhibitory effect Effects 0.000 description 1
- PNDPGZBMCMUPRI-UHFFFAOYSA-N iodine Chemical compound II PNDPGZBMCMUPRI-UHFFFAOYSA-N 0.000 description 1
- 230000007935 neutral effect Effects 0.000 description 1
- 239000007800 oxidant agent Substances 0.000 description 1
- 238000005201 scrubbing Methods 0.000 description 1
- 229910000030 sodium bicarbonate Inorganic materials 0.000 description 1
- 235000017557 sodium bicarbonate Nutrition 0.000 description 1
- SUKJFIGYRHOWBL-UHFFFAOYSA-N sodium hypochlorite Chemical compound [Na+].Cl[O-] SUKJFIGYRHOWBL-UHFFFAOYSA-N 0.000 description 1
- 238000005406 washing Methods 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C7/00—Purification; Separation; Use of additives
- C07C7/11—Purification; Separation; Use of additives by absorption, i.e. purification or separation of gaseous hydrocarbons with the aid of liquids
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Engineering & Computer Science (AREA)
- Analytical Chemistry (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Water Supply & Treatment (AREA)
- Electrolytic Production Of Non-Metals, Compounds, Apparatuses Therefor (AREA)
Description
Verfahren zur Reinigung von Azetylen. Es ist bekannt, dass die Verunreinigungen des Azetylens, wie Phosphorwasserstoff und Schwefelwasserstoff, aus dem Azetylen durch v(,r.-;cliiedene Oxydationsmittel, wie Chlor k,alk, Ily pochlorit, Chlor, Brom, Jod, Chrom säure usw., entfernt werden können.
Weiter ist bekannt, dass verdünnte Lösun gen von unterchlorigsauren Salzen nur sehr wenig auf Phosphorwasserstoff einwirken, während im Gegensatz hierzu konzentrierte 1=lypochloritlösungen und vor allem freie un terchlorierte Säure, einesteils zwar die Ver unreinigungen vollkommen entfernen, andern teils aber auch kräftig auf Azetylen einwir ken, derart, da.ss es zur Explosion kommen kann.
(V ergl. Vogel: Das Azetylen", 1911. Seite 26 und 60.) Aus diesem Grunde haben Hypochloritlaugen zur Reinigung von Azety len in der Technik bisher keine dauernde Ver wendung gefunden.
Wir haben nun gefunden, dass verhältnis mässig konzentrierte Lösungen von Hypo- chloriten ihre Fähigkeit mit Azetylen zu rea gieren und damit ihre ExplosionsgeNihrlich- heit vollkommen verlieren, wenn man durch geeignete Zusätze zur Lösung dafür sorgt, dass die Lösung keine erhebliche Konzentra tion an freier Hypochlorsäure erreichen kann.- Als solche Zusätze kommen Salze schwacher, d. h. wenig dissoziierter Säuren in Betracht; als besonders günstig erwies sich ein Zusatz von Alkalibikarbonat.
Dieser eigentümlichen, explosionshemmen den Wirkung des Bikarbonates liegen fol- ;ende Tatsachen zu Grunde: Infolge der Bildung verschiedener Phos phorsäuren während der Azetylenreinigung wird die ursprüngliche neutrale Hypochlorit- lösung sauer; bei länger dauernder Reinigung kann sich also eine erhebliche Konzentration .an freier Hypochlorsäure einstellen. Diese freie Hypochlorsäure und nicht das Hypo- chlorit selbst bildet infolge von Chlorabspal tung die Ursache der Explosionen.
Durch Zu satz der entsprechenden Menge .Alkalibikar- bonat werden die Phosphorsäuren spontan in dem Masse neutralisiert, wie sie sich bilden, während IKohlen.dioxyd zum Teil aus der ZVaschlösung entweicht. (Teil die Kohlen säure eine sehr schwache Säure ist, kann sich in Gegenwart von kohlensauren. Salzen nur eine äusserst geringe Konzentration an freier unterchloriger Säure einstellen.
Entsprechend dieser geringen Konzentration erweist sich nun,das gereinigte Gas als vollkommen ohlor- frei, während beim Arbeiten ohne Bikarbonat- zusatz im gereinigten Gas immer Chlor vor handen ist.
Man wählt die Konzentration der Lösun gen -derart, dass einerseits die Verunreinigun gen rasch entfernt, anderseits aber Azetylen nicht angegriffen wird.
Die zur Gasreinigung, verwendete Lösung, -elche bis auf einen Gehalt von zirka 2 s ,aktivem Chlor pro Liter ausgebraucht wer den kann, lässt sich auf elektrolytischem Wege mit irgend einem der bekannten Elektrolyt bleiclilauge-Verfa.hren regenerieren.
<I>Beispiel:</I> 1000 Liter einer Lösung von Natrium- hypochlorit, enthaltend zirka 25 g aktives Chlor pro Liter, werden mit einem Zusatz von 12 kg Natriumbika.rbonat versetzt. Die so bereitete Lösung wird durch eine der be kannten Gaswaschvorrichtungen geschickt. Ein Reaktionsvolumen von 3 m$ gestattet so die stündliche Reinigung von 100 in' Azety len. Das vorher 0,15 Volumenprozent Phos phorwasserstoff enthaltende Azetylen erwies sich .als praktisch phosphorfrei. Chlor konnte in dem Gase nicht na@chgewieseii werden.
Die Lösung wird regeneriert, indem man sie nach einem der bekannten Verfahren der Elektrolyse unterwirft, dabei wird mit Vor teil ,mit Gra.phitanoden und mit einem Zusatz von Kaliumchromat gearbeitet.
Process for purifying acetylene. It is known that the impurities in acetylene, such as hydrogen phosphide and hydrogen sulfide, are removed from the acetylene by means of various oxidizing agents such as chlorine, alk, chlorine, chlorine, bromine, iodine, chromic acid, etc. can be.
It is also known that dilute solutions of hypochlorous acid salts have very little effect on hydrogen phosphide, while in contrast to this, concentrated 1 = hypochlorite solutions and, above all, free un-chlorinated acid, partly remove the impurities completely, but partly also act vigorously on acetylene in such a way that an explosion can occur.
(Compare Vogel: Das Acetylen ", 1911. Pages 26 and 60.) For this reason, hypochlorite liquors for cleaning acetylenes have not been used continuously in technology.
We have now found that relatively concentrated solutions of hypochlorites are able to react with acetylene and thus completely lose their risk of explosion if suitable additives are used to ensure that the solution does not contain a significant concentration of free hypochlorous acid - As such additives come weaker salts, i.e. H. slightly dissociated acids into consideration; The addition of alkali bicarbonate proved to be particularly beneficial.
This peculiar, explosion-inhibiting effect of bicarbonate is based on the following facts: As a result of the formation of various phosphoric acids during acetylene purification, the original, neutral hypochlorite solution becomes acidic; If cleaning takes longer, a considerable concentration of free hypochlorous acid can develop. This free hypochlorous acid and not the hypochlorite itself is the cause of the explosions as a result of the release of chlorine.
By adding the appropriate amount of alkali carbonate, the phosphoric acids are spontaneously neutralized to the extent that they are formed, while some carbon dioxide escapes from the washing solution. (Part of the carbonic acid is a very weak acid, and in the presence of carbonic acid salts, only an extremely low concentration of free hypochlorous acid can be established.
Corresponding to this low concentration, the cleaned gas turns out to be completely free of chlorine, while chlorine is always present in the cleaned gas when working without the addition of bicarbonate.
The concentration of the solutions is chosen in such a way that, on the one hand, the impurities are removed quickly, but on the other hand, acetylene is not attacked.
The solution or solution used for gas cleaning can be used up to a content of approx. 2 s of active chlorine per liter, can be regenerated electrolytically with any of the known electrolyte lead lye processes.
<I> Example: </I> 1000 liters of a solution of sodium hypochlorite, containing approx. 25 g of active chlorine per liter, are mixed with an addition of 12 kg of sodium bicarbonate. The solution prepared in this way is sent through one of the known gas scrubbing devices. A reaction volume of 3 m $ allows the hourly cleaning of 100 in 'acetyls. The acetylene, which previously contained 0.15 percent by volume of hydrogen phosphide, proved to be practically phosphorus-free. Chlorine could not be detected in the gas.
The solution is regenerated by subjecting it to electrolysis according to one of the known processes, which involves working with advantages, with graphite anodes and with the addition of potassium chromate.
Claims (1)
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CH97595T | 1921-08-18 |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CH97595A true CH97595A (en) | 1923-02-01 |
Family
ID=4355349
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CH97595D CH97595A (en) | 1921-08-18 | 1921-08-18 | Process for purifying acetylene. |
Country Status (1)
| Country | Link |
|---|---|
| CH (1) | CH97595A (en) |
-
1921
- 1921-08-18 CH CH97595D patent/CH97595A/en unknown
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| DE2130945C3 (en) | Process for removing mercury vapor from gases contaminated with it | |
| DE19721301C1 (en) | Hydrolysis of alkyl mono:halide to corresponding alcohol | |
| DE69200006T2 (en) | Process for the electrolytic production of alkali metal chlorate and chemical auxiliary compounds. | |
| DE3614005C2 (en) | ||
| DE2816772A1 (en) | METHOD FOR PURIFYING Aqueous SODIUM CHLORIDE SOLUTION | |
| DE2442828C2 (en) | Process for the treatment of waste gas or furnace gas containing nitrogen oxide | |
| DE1193015B (en) | Device for absorbing acidic or alkaline components from gas mixtures | |
| DE3637939A1 (en) | METHOD FOR PRODUCING ALKALINE HYDROXIDE, CHLORINE AND HYDROGEN BY ELECTROLYSIS OF AN AQUEOUS ALKALICHLORIDE SOLUTION IN A MEMBRANE CELL | |
| DE4326128A1 (en) | Process for the electrolysis of an aqueous potassium chloride solution | |
| DE2510842A1 (en) | METHOD FOR RECOVERY OF IODINE | |
| DE2545342A1 (en) | METHOD FOR THE ABSORPTION OF CHLORINE | |
| CH97595A (en) | Process for purifying acetylene. | |
| DE2919996A1 (en) | PROCESS FOR THE CONTINUOUS PRODUCTION OF ALKALIMETAL CHLORATES | |
| DE2124045C3 (en) | Process for the electrolytic Her position of pure chlorine, hydrogen and pure concentrated alkali metal phosphate solutions and electrolyzer cell to carry out the process | |
| DE391382C (en) | Process for purifying acetylene | |
| DE1061613B (en) | Process for the regeneration of alkali sulphite or alkali bisulphite pulp waste liquors | |
| DE3729669A1 (en) | METHOD FOR PRODUCING ALKALINE METAL NITRATES | |
| DE1812723A1 (en) | Method for removing hypochlorite from an electrolytic cell | |
| DE115677C (en) | ||
| DE1767896A1 (en) | Process for cleaning metal chloride salts | |
| DE328211C (en) | Process for the production of chlorates, bromates and iodates | |
| DE347368C (en) | Process for the electrolytic production of alkali perborates | |
| DE531112C (en) | Process for detinning tinplate waste or other tin-containing material | |
| DE157150C (en) | ||
| AT16959B (en) | Process for the electrolytic preparation of the permanganates of alkaline earth, earth and heavy metals. |