DE748056C - Process for the recovery of hydrogen sulfide and carbon disulfide from contaminated viscose hair with simultaneous evaporation of the same - Google Patents

Process for the recovery of hydrogen sulfide and carbon disulfide from contaminated viscose hair with simultaneous evaporation of the same

Info

Publication number
DE748056C
DE748056C DES145351D DES0145351D DE748056C DE 748056 C DE748056 C DE 748056C DE S145351 D DES145351 D DE S145351D DE S0145351 D DES0145351 D DE S0145351D DE 748056 C DE748056 C DE 748056C
Authority
DE
Germany
Prior art keywords
hydrogen sulfide
bath
recovery
contaminated
carbon disulfide
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.)
Expired
Application number
DES145351D
Other languages
German (de)
Inventor
Dr-Ing Albrecht Siehr
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
DIETRICH CHRISTIAN SIEHR
DORIS RENATE SIEHR
JOACHIM ALBRECHT SIEHR
JOHANNE GEN HANNA MATHILDE PAU
WOLFGANG ERNST LUDWIG SIEHR
Original Assignee
DIETRICH CHRISTIAN SIEHR
DORIS RENATE SIEHR
JOACHIM ALBRECHT SIEHR
JOHANNE GEN HANNA MATHILDE PAU
WOLFGANG ERNST LUDWIG SIEHR
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 DIETRICH CHRISTIAN SIEHR, DORIS RENATE SIEHR, JOACHIM ALBRECHT SIEHR, JOHANNE GEN HANNA MATHILDE PAU, WOLFGANG ERNST LUDWIG SIEHR filed Critical DIETRICH CHRISTIAN SIEHR
Priority to DES145351D priority Critical patent/DE748056C/en
Application granted granted Critical
Publication of DE748056C publication Critical patent/DE748056C/en
Expired legal-status Critical Current

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Classifications

    • DTEXTILES; PAPER
    • D01NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
    • D01FCHEMICAL FEATURES IN THE MANUFACTURE OF ARTIFICIAL FILAMENTS, THREADS, FIBRES, BRISTLES OR RIBBONS; APPARATUS SPECIALLY ADAPTED FOR THE MANUFACTURE OF CARBON FILAMENTS
    • D01F13/00Recovery of starting material, waste material or solvents during the manufacture of artificial filaments or the like
    • D01F13/02Recovery of starting material, waste material or solvents during the manufacture of artificial filaments or the like of cellulose, cellulose derivatives or proteins
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P70/00Climate change mitigation technologies in the production process for final industrial or consumer products
    • Y02P70/50Manufacturing or production processes characterised by the final manufactured product
    • Y02P70/62Manufacturing or production processes characterised by the final manufactured product related technologies for production or treatment of textile or flexible materials or products thereof, including footwear

Landscapes

  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Textile Engineering (AREA)
  • Treating Waste Gases (AREA)

Description

Verfahren zur Rückgewinnung von Schwefelwasserstoff und Schwefelkohlenstaff aus verunreinigten Viskosefällbädern unter gleichzeitiger Eindampfung derselben In den nach dein Vi-skoseverfahren arbeitenden Kunstseide-, Zelljute-, Zellfolie- und ZellwG1lefabri,'k#en -wird beim Verformen der Viskose das Fällbad fortschreitend mit Wasser verdünnt und gleichzeitig mit wertvollen, aber gesundheitsschädlichen Stoffen, wie Schwefelwasserstoff und Sch-,vefelkohIenstoff, angereichert. Es -ergibt sich sornit die Aufgabe, das Fällbad von dem überschüssigen Wasser zu befreien und die ihm zugeführten wertvollen Stoffe zurückzuggewinnen. Von diesen Stoffen hat man schon die Badflüssigkeit durch starke Bel üftung befreit, sie gehen alsdann aber verlor-en, da sle in der Abluft in so starker* Verdünnung auftreten, daß ihre Wiedergewinnting nicht möglich ist. Diesen Nachteil versuchte man dadurch = vermeiden, daß man die Belüftung der Badflüssigkeit mit einer stark begrenzten Luftmenge bewirkt. Das hat man 4a,durch erreicht, daß man die verunreinigte Flüssigkeit in den Fällbadbottichen unter- Vakuum setzte und alsdann die begrenzte Luftmenge in feiner Verteilung hindurchleitete. Sie enthielt alsdann die Schwefelverbindungen in ausreichend starker Konzentration, um eine Wiedergewinnung zu ermöglichen. Gleichzeitig erfolgte auch eine Eindampfung des Bades insoweit, als die hindurchgepreßteLuft dieses mit Wasserdampf beladen verließ.Process for the recovery of hydrogen sulfide and carbon disulfide from contaminated viscose precipitation baths with simultaneous evaporation of the same In the rayon, cell jute and cell foil that work according to your viscose process and ZellwG1lefabri, 'k # en -when the viscose is deformed, the precipitation bath progresses diluted with water and at the same time with valuable but harmful to health Substances such as hydrogen sulfide and carbon dioxide, enriched. It -does sornit the task of freeing the precipitation bath from the excess water and to recover the valuable substances supplied to it. Has of these substances if the bath liquid is already freed by strong ventilation, they then go but lost, since they appear in the exhaust air in so great a dilution that their Recovery is not possible. The attempt was made to avoid this disadvantage by that the ventilation of the bath liquid is effected with a very limited amount of air. This has been achieved 4a by putting the contaminated liquid in the felling bath tubs put under vacuum and then passed through the limited amount of air in fine distribution. It then contained the sulfur compounds in a sufficiently high concentration to enable recovery. Evaporation also took place at the same time of the bath insofar as the air forced through it loads it with water vapor left.

Geggenstandder Erfindung ist eine Weiterbildung dieses Verfahrens, die seine Wirtschaftlichkeit erhöht und dabei eine be#sonders wirksarnfe Entgasung , des Bades gewährleistet, so-,vie eine Eindampfung bis zu. der gewünschten Konzentration gestattet. Die Erfindung liegt darin, daß zur Badbelüftung heißes Gas benutzt und dieses im Kreislauf geführt wird. Bei dem bekannten niedrigen Siedepunkt des Schwefelkohlenstoffes wird er von dem h,cißen Gas besonders gut aus Flüssigkeiten ausgetrieben, und die Kreislaufführung des Belüftungsgases ermöglicht die el el Benutzung einer geringen Gesamtmenge., so daß in ihm die Konzentration der mitgefübrten Schwefelverbindungen besonders hoch ist. Der Gaskreislauf ermöglicht ferner die wirtschaftliche Anwendung hoher Temperaturen, da Wärrneverluste fortfallen. Schließlich erfolgt wegen der hohen Temperaturen auch eine besonders wirksame Eindampfung des Bades, und diese kann auf Grund des Gaskreislaufes bis zu jedem gewünschten Konzentrationsgrade der Badflüssigkeit fortgesetzt werden.Geggenstandder invention is a development of this method, which increases its efficiency and doing a # Sonder be wirksarnfe degassing of the bath ensures so-, vie an evaporation up to. the desired concentration. The invention lies in the fact that hot gas is used for bath ventilation and this is circulated. With the known low boiling point of carbon disulfide, the hot gas expels it particularly well from liquids, and the circulation of the aeration gas enables a small total amount to be used, so that the concentration of the sulfur compounds that are carried along is particularly high in it. The gas cycle also enables high temperatures to be used economically, since there are no heat losses. Finally, because of the high temperatures, there is also a particularly effective evaporation of the bath, and this can be continued up to any desired degree of concentration of the bath liquid due to the gas cycle.

Zur Durchführung des Verfahrens wird das Gas in heißem Zustande in das Fällbad eingeführt und dabei z. B. durch ein keramisches Filter geblasen, so daß ein fein verteilter Gasstrornentstelit. Damit die Gasverteilung im Bad gleichmäßig erfolgt, wird über dem Gasverteiler eine Vorrichtun, '-, z. B. ein beiderseits offenes Rohr, angeordnet. Infolge der feinen Gasverteilung und der hohen Temperatur des Gases lindet ein wirksames Austreiben der Schwefelverbindungen und eine sehr starke Verdampfung des in der Badflüssigkeit enthalteneii Wassers statt. Zur Verstärkun-, der Wirkun- ist der über dein Bade liegende Raum evakuiert. Nachdem das Gas durch die Fällbadflässigkeit hindurchgeströmt ist, wird es abgesaugt, durch Kondensations- und Ab- oder Adsorptionsvorrichtungen geleitet und alsdann dem Fällbad wieder zugeführt. Als KonJensationsvorrichtungen können z. B. Kühler verwendet werden, als Ad- und Absorptionsvorrichtun-gen Gaswäscher oder regenerierbare aktive Kohlefilter. In diesen Vorrichtungen gibt das Gas seinen Gehalt an Wasser, Schvefelkohlenc toff undSchwefelwasserstoff ab und tritt, von .idies#n Stoffen weitgehend befreit, wieder in fein verteilter Form in das Fällbad ein.To carry out the process, the gas is introduced into the precipitating bath while it is hot. B. blown through a ceramic filter, so that a finely divided gas flow entstelit. So that the gas is distributed evenly in the bath, a device is placed over the gas distributor, '-, z. B. a tube open on both sides arranged. As a result of the fine gas distribution and the high temperature of the gas, the sulfur compounds are effectively expelled and the water contained in the bath liquid is very strongly evaporated. To strengthen the effect, the room above your bath has been evacuated. After the gas has flowed through the precipitation bath liquid, it is sucked off, passed through condensation and absorption or adsorption devices and then fed back into the precipitation bath. As KonJensationsvorrichtungen z. B. Coolers can be used as adsorption and absorption devices gas scrubbers or regenerable active carbon filters. In these devices, the gas releases its water, carbon and hydrogen sulphide content and, largely freed of these substances, re-enters the precipitation bath in finely divided form.

Claims (1)

PATENTANSPRUCH: Verfahren zur Rückgewinnung von Sch-wefelkohlenstoff und Schwefelwasserstoff aus verunreinigten Viskosefällbädern unter gleichzeitigem Eindampfen derselben, wobei durch die unter Vakuum stehende Badflüssigkeit ini Fällbadbottich fein verteiltes Gas geleitet wird, das man dann in Kondensations- oder AdsorptionsvorrieWungen von dem aus dem Bad mitgenommenen Schwefelkoblenstoff, Schwefelwasserstoff und Wasser befreit, dadurch gekennzeichnet, daß man heißes Gas unter Kreislaufführun- verwendet. kn Zur Abgrenzung des Anmüldungsgegenstan-des vom Stand der Technik sind im Erteilungsverfahren folgende Druckschriften in Betracht gezogen worden: französische Patentschrift Nr. 859 682; britische 498799. PATENT CLAIM: Process for the recovery of sulfur carbon and hydrogen sulfide from contaminated viscose precipitation baths with simultaneous evaporation of the same, whereby finely divided gas is passed through the bath liquid under vacuum in the precipitation bath tub, which is then in condensation or adsorption devices of the carbon disulfide taken from the bath, Freed hydrogen sulfide and water, characterized in that hot gas is used with circulation. kn Definition of the Anmüldungsgegenstan-the following publications are prior art in the grant procedure envisioned: French Patent No. 859,682;. british 498799.
DES145351D 1941-05-15 1941-05-16 Process for the recovery of hydrogen sulfide and carbon disulfide from contaminated viscose hair with simultaneous evaporation of the same Expired DE748056C (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
DES145351D DE748056C (en) 1941-05-15 1941-05-16 Process for the recovery of hydrogen sulfide and carbon disulfide from contaminated viscose hair with simultaneous evaporation of the same

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
DE228895X 1941-05-15
DES145351D DE748056C (en) 1941-05-15 1941-05-16 Process for the recovery of hydrogen sulfide and carbon disulfide from contaminated viscose hair with simultaneous evaporation of the same

Publications (1)

Publication Number Publication Date
DE748056C true DE748056C (en) 1944-10-25

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DES145351D Expired DE748056C (en) 1941-05-15 1941-05-16 Process for the recovery of hydrogen sulfide and carbon disulfide from contaminated viscose hair with simultaneous evaporation of the same

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Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB498799A (en) * 1937-05-18 1939-01-13 Glanzstoff Ag An improved process for expelling and recovering carbon disulphide vapours and other gases or vapours from liquids, more particularly from spinning and washing waters of the viscose artificial silk and cellulose wool industries
FR859682A (en) * 1944-01-22 1940-12-24 Comptoir Textiles Artificiels Viscose spinning bath treatment process

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB498799A (en) * 1937-05-18 1939-01-13 Glanzstoff Ag An improved process for expelling and recovering carbon disulphide vapours and other gases or vapours from liquids, more particularly from spinning and washing waters of the viscose artificial silk and cellulose wool industries
FR859682A (en) * 1944-01-22 1940-12-24 Comptoir Textiles Artificiels Viscose spinning bath treatment process

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