DE315262C - - Google Patents
Info
- Publication number
- DE315262C DE315262C DENDAT315262D DE315262DA DE315262C DE 315262 C DE315262 C DE 315262C DE NDAT315262 D DENDAT315262 D DE NDAT315262D DE 315262D A DE315262D A DE 315262DA DE 315262 C DE315262 C DE 315262C
- Authority
- DE
- Germany
- Prior art keywords
- gases
- heavy
- containers
- insulator
- container
- 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.)
- Active
Links
- 239000007789 gas Substances 0.000 claims description 19
- 239000012212 insulator Substances 0.000 claims description 10
- 238000004140 cleaning Methods 0.000 claims description 5
- 239000007788 liquid Substances 0.000 claims description 2
- 238000001556 precipitation Methods 0.000 description 4
- UHOVQNZJYSORNB-UHFFFAOYSA-N benzene Chemical compound C1=CC=CC=C1 UHOVQNZJYSORNB-UHFFFAOYSA-N 0.000 description 2
- QGJOPFRUJISHPQ-UHFFFAOYSA-N carbon bisulphide Chemical compound S=C=S QGJOPFRUJISHPQ-UHFFFAOYSA-N 0.000 description 2
- 238000001816 cooling Methods 0.000 description 2
- RTZKZFJDLAIYFH-UHFFFAOYSA-N diethyl ether Chemical compound CCOCC RTZKZFJDLAIYFH-UHFFFAOYSA-N 0.000 description 2
- 230000036633 rest Effects 0.000 description 2
- YXFVVABEGXRONW-UHFFFAOYSA-N toluene Chemical compound CC1=CC=CC=C1 YXFVVABEGXRONW-UHFFFAOYSA-N 0.000 description 2
- PGMYKACGEOXYJE-UHFFFAOYSA-N Amyl acetate Chemical compound CCCCCOC(C)=O PGMYKACGEOXYJE-UHFFFAOYSA-N 0.000 description 1
- 229940072049 amyl acetate Drugs 0.000 description 1
- 239000000356 contaminant Substances 0.000 description 1
- 238000009792 diffusion process Methods 0.000 description 1
- 239000000428 dust Substances 0.000 description 1
- 238000001704 evaporation Methods 0.000 description 1
- 239000000945 filler Substances 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- UFHFLCQGNIYNRP-UHFFFAOYSA-N hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 1
- 238000005507 spraying Methods 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B03—SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
- B03C—MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
- B03C3/00—Separating dispersed particles from gases or vapour, e.g. air, by electrostatic effect
- B03C3/34—Constructional details or accessories or operation thereof
- B03C3/66—Applications of electricity supply techniques
- B03C3/70—Applications of electricity supply techniques insulating in electric separators
Description
Die vorliegende Erfindung hat den Zweck, bei elektrischen Gasreinigungen die Isolatoreh, welche das System. der sprühenden Elektroden tragen, vor Staub und anderen Verunreinigungen zu schützen. Es wird dies dadurch erreicht, daß man dafür sorgt, daß die Isolatoren gar nicht mit dem zu behandelnden Gase in Berührung kommen und daß auch nicht der geringste Luftzug etwas vonThe present invention has the purpose, in electrical gas cleaning, the Isolatoreh, which the system. of the spraying electrodes, from dust and others To protect contaminants. It becomes this achieved by making sure that the isolators do not interfere with the treated Gases come into contact and that not even the slightest draft of air has anything to do with
to diesem Gase an die Isolatoren heranbringt. Zu diesem Zwecke umgibt man die Isolatoren mit völlig ruhender Luft.. Man verlegt sie in aufrechte röhren- oder kastenförmige Behälter, die entweder an ihrem oberen Ende mit dem Niederschlagsraume verbunden und unten geschlossen sind oder umgekehrt.to this brings gases to the insulators. For this purpose, the isolators are surrounded by completely still air. They are laid in upright tubular or box-shaped containers either at their top are connected to the precipitation area and closed at the bottom or vice versa.
Eine Form der ersten Art zeigt die Fig. 1. In solchen abwärts gerichteten Behältern ruht die Luft, wenn sie. spezifisch1 schwerer ist als die Luft des Hauptraumes. Man erreicht diesen Zweck, wenn man den Isolatorenbehälter mit einem schweren Gase füllt oder ihn besonders kühlt. Ist die Temperatur des Niederschlagsraumes vielleicht eine höhere, so ist eine besondere Kühlung überflüssig.A form of the first type is shown in FIG. 1. In such downward-facing containers the air rests when they. specifically 1 is heavier than the air in the main room. This purpose can be achieved by filling the insulator container with a heavy gas or by cooling it specially. If the temperature of the precipitation area is perhaps higher, special cooling is superfluous.
■ Die Isolatorenbehälter dieser Art können übrigens auch unter, über und in dem Hauptraume liegen. Soll ein Behälter oberhalb des Niederschlagsräumes liegen, so nimmt man■ The insulator containers of this type can also be placed under, above and in the main room lie. If a container is to be located above the precipitation area, then one takes
30. ihn am1 besten doppelt (Fig. 2).30 him best at 1 twice (Fig. 2).
Die Methode läßt sich umkehren. Bekanntlich entweicht Wasserstoffgas aus einem umgekehrten Zylinder nicht. Strecken wir den Isolatorenbehälter also aufwärts, füllen ihn mit einem leichten Gase oder verdünnen die Luft in ihm durch stärkere Erwärmung, so ruht das Gas in ihm ebenfalls. Dabei können die Isolatoren i (Fig. 3 und 4) entweder ganz im Innern der Behälter liegen oder auch einen Teil ihrer Wandung ausmachen.The method can be reversed. It is well known that hydrogen gas does not escape from an inverted cylinder. So if we stretch the insulator container upwards, fill it with a light gas or dilute the air in it by heating it up, the gas also rests in it. The insulators i (FIGS. 3 and 4) can either lie entirely inside the container or make up part of their walls.
Die Füllung des Isolatorenbehälters mit einem schweren oder leichten Gase hat nichts zu tun mit dem ununterbrochenen Strom reinen Gases, den Cottrell über die eben- · falls außerhalb des Niederschlagsraumes angeordneten Isolatoren leitet. Bei dem vorliegenden Verfahren genügt es, von Zeit zu Zeit etwas Gas nachzufüllen, um den durch Diffusion entstandenen Verlust des .sonst völlig ruhenden Gases zu ersetzen.The filling of the insulator container with a heavy or light gas does nothing to do with the uninterrupted flow of pure gas, which Cottrell via the if conducts insulators arranged outside the precipitation area. In the present method, it is sufficient from time to time Time to refill some gas to avoid the loss of the .otherwise caused by diffusion to replace completely dormant gas.
Die Füllung der Isolatorenbehälter: mit schweren oder leichten Gasen kann auch dadurch geschehen, daß man kleinere Mengen gewisser Flüssigkeiten in den Behältern zur Verdampfung bringt. So liefert Äther einen Dampf von der Dichte 2,54 (Luft = 1), Schwefelkohlenstoff von 2,61, Benzol von 2,68, Toluol von 3,16, Amylacetat von 4,88. Alle diese schweren Dämpfe eignen sich als; Füllmittel abwärts gestreckter,- unten geschlössen«· Behälter. Handelt es sich umgekehrt um die Füllung eines aufwärts gerichteten Behälters mit einem leichten Gase, so empfiehlt sich, wenigstens bei etwas höherer Temperatur, Wasserdampf (Dichte· 0,622). - .■■..'The filling of the insulator container: with heavy or light gases can also result happen that you have smaller amounts of certain liquids in the containers for Brings evaporation. Ether delivers a vapor with a density of 2.54 (air = 1), Carbon disulfide of 2.61, benzene of 2.68, toluene of 3.16, amyl acetate of 4.88. All of these heavy vapors are suitable as; Filler stretched downwards - closed at the bottom «· Container. Conversely, if it is a matter of filling an upward-facing container with a light gas, it is recommended, at least at a slightly higher temperature, to use water vapor (density 0.622). -. ■■ .. '
Claims (3)
Publications (1)
Publication Number | Publication Date |
---|---|
DE315262C true DE315262C (en) |
Family
ID=568027
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
DENDAT315262D Active DE315262C (en) |
Country Status (1)
Country | Link |
---|---|
DE (1) | DE315262C (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4846857A (en) * | 1986-10-14 | 1989-07-11 | Mitsubishi Jukogyo Kabushiki Kaisha | Electric dust collector with electrode supporter therefor |
-
0
- DE DENDAT315262D patent/DE315262C/de active Active
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4846857A (en) * | 1986-10-14 | 1989-07-11 | Mitsubishi Jukogyo Kabushiki Kaisha | Electric dust collector with electrode supporter therefor |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
DE1935763C3 (en) | Process for the production of flat glass and device for carrying out the process | |
DE315262C (en) | ||
DE2026904A1 (en) | Procedure for the storage of a hazardous material | |
EP3539641A1 (en) | Method for after-treatment of regeneration waste gas | |
DE3520671C2 (en) | ||
DE3141484A1 (en) | "TWO-STAGE LIQUID BED REGENERATOR" | |
DE871291C (en) | Heat transfer system and method for heat transfer | |
DE4441199B4 (en) | Apparatus and method for cleaning gases to be introduced into a laser chamber | |
EP0547400B1 (en) | Process for removing H2S from gases | |
EP3932521A1 (en) | Process for purifying a crude gas stream containing sulphur components and hydrocarbons | |
EP3921063A1 (en) | Two-stage method for recovering halogenated hydrocarbons | |
DE102016111179B4 (en) | Device and method for the pretreatment of a gas | |
DE4227416C1 (en) | Hydrocarbon esp. gasoline fumes recovery from air - involves condensation using liq. coolant prior to adsorption | |
DE2337961A1 (en) | PROCEDURE FOR AMMONIA MANAGEMENT IN COPY DEVICES | |
DE495429C (en) | Separation of gas mixtures by liquefaction | |
DE8213351U1 (en) | Sterilizing containers for medical instruments | |
DE3802997A1 (en) | Method and apparatuses for separating off vapours of organic solvents or other pollutants from air by adsorption | |
DE2343081A1 (en) | Reducing vapourised petrol losses from storage tanks - by cooling air-vapour mixt. in tubular cooler and returning condensate to tank | |
DE517842C (en) | Method and device for the elimination of chemically active gases in oil containers, in particular for electrical apparatus | |
DE2950983A1 (en) | ADSORBER FOR PURIFYING GASES | |
DE4024271A1 (en) | Assembly for removal or redn. of ozone content in gas - by passing gas through vessel in which energy is introduced and heating | |
DE459344C (en) | Process for drying fuels | |
DE4306064A1 (en) | Method and plant for the residual emptying and degassing of tank wagons and tanks for the transport or storage of liquefied gas and for the recovery of the liquefied gas | |
DE4224950A1 (en) | Evaluating emissions of gas return arrangements in vehicle fuel tank filling systems - involves taking into account properties of inert gas and gas vol. development caused by fuel displacement | |
DE10311558B3 (en) | Device for extinguishing fire comprises treatment stage for exhaust gases, quenching/washing stage for exhaust gases, transporting devices and pipelines for forming gas circulation |