US666044A - Method of filtering steam. - Google Patents

Method of filtering steam. Download PDF

Info

Publication number
US666044A
US666044A US1845400A US1900018454A US666044A US 666044 A US666044 A US 666044A US 1845400 A US1845400 A US 1845400A US 1900018454 A US1900018454 A US 1900018454A US 666044 A US666044 A US 666044A
Authority
US
United States
Prior art keywords
steam
filtering
cylinders
agalite
filtering steam
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 - Lifetime
Application number
US1845400A
Inventor
William Henry Barr
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.)
Individual
Original Assignee
Individual
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 Individual filed Critical Individual
Priority to US1845400A priority Critical patent/US666044A/en
Application granted granted Critical
Publication of US666044A publication Critical patent/US666044A/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Images

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J23/00Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
    • B01J23/38Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of noble metals
    • B01J23/40Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of noble metals of the platinum group metals
    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01BNON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B5/00Water

Definitions

  • Figure l is a sectional elevation ofa single unit apparatus for filtering and deodorizing steam.
  • Fig. 2 is a sectional elevation of .an apparatus suitable for the treatment of very large'yolumes of steam.
  • Fig. 3 is a plan of Fig. 2 with the' cover removed.
  • Fig. 4 is an enlarged detail -view of a portion of one of 30 jshown in Figs. 2 and 3.
  • the apparatus consists of a pressure-proof casing v a, carried by asuitablestand b.
  • A'cov'er c is supplied, secured by means of hinged bolts c', While a dis-k c2 of asbestos provides'a fluid- "tight joint between the lid or cover c and the casing a.
  • Tol'the cov'er c is secured a filterbed d, which consists of a perforated metallic tube.
  • I employ any suitable number of filteringcylinders,.according to the volume. of steam to treated, and mount such filtering-cylinders in concentric circles, as shown in the plauvview- Fig. 3, Within avpressure-p'roof cas- ⁇ 44fing g.
  • the vcylinders deliver thel purified arrangement forsixty-one cylinders.
  • FIGs. 2 and 3 show such an A lid or coveri is secured to the casing g by means of swing-belts il', which cover also carries a balance-weight hookj, pressure-gage lc, and
  • the lter-beds each consist vof a .central perforated drainage-tube fm, screwed and expandedin the diaphragm -plate "n, which forms -a roo-l ⁇ to the reservoir or receiver h.
  • Thepe'r-forated drainagetubes n serve' to carry and support pervious cylinders'o, a concentric circulating-space being provided by distance-pieces p.
  • the pervious cylinders o are wrapped with mercerized uustretched cot- 'ton cloth, ⁇ the ends of which are tucked with.- in the cylinders yo and the Whole secured in' ⁇ Aposition by meansv of cap-nuts y ⁇ p',whieh' screw'.
  • the cap-nuts p may be unscrewed and the outer cylinders o removed to Wash offv the dirty iltering-earth,or the filter-beds may be washed n situ by a .reversed vcurrent of clean water delivered through the receiver h,whie h throwsoii the deposit of dirtyltering-earths, the deposit being ⁇ removed,'from thecasingfg by Way of the flush-pipe r. to an enlarged scalea portion of the filter-bed.

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Inorganic Chemistry (AREA)
  • Engineering & Computer Science (AREA)
  • Materials Engineering (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Extraction Or Liquid Replacement (AREA)

Description

` Patented Jan. l5, |90I. W. H. BARR. METHOD 0F FILTERING STEAM.
(Application med my 29, 1960.)
www
(Na Model.)
,.UNITEID STAT-Es AT1-NT OFFICE.
WILLIAM HENRY BARR, or BURY, ENGLAND.
METHOD -oF FlLTpEfRiNG STEAM.
A- SPECIFICATION fermijng part of Letters Patent No. 666,044, dated January'ls, 1901,.
application ledllllay 29, 1900. Serial No. 12,454. (No specimens.) Y
Taal? whQm tn/bay concern.: 'I y v Beit known that I, VV'ILLIAM HENRYBARR, a subject of the Queen of Great Britain and. Ilieland,'residing-at", Bury, iuthe count-y of Lancaster,`England,'have invented certain I newand useful Improveinentsin Methods of andpApparatus for Filtering and Deodorizing Steam,(for which I have made application for patent `in Great Britain, No.` 13,128, dated June 24,'1899,)'of"which the following is a 'speciflcation.,y i y My invention relates toa method of and apparat-us for use in filtering anddeodorizing steam, by means of which exhaust or live steam maybe filtered to remove oily particles,
. moisture of condensation, and foreign mataccompanying drawings show tersA held in suspension'. Further, when required, bad smells due'to hydrogen sulfid or to-otherrvolatile organic substances may be removed and the steam thus deodorized. The the apparatus devised for this purpose. v
Figure l is a sectional elevation ofa single unit apparatus for filtering and deodorizing steam. Fig. 2 is a sectional elevation of .an apparatus suitable for the treatment of very large'yolumes of steam. Fig. 3 is a plan of Fig. 2 with the' cover removed. Fig. 4 is an enlarged detail -view of a portion of one of 30 jshown in Figs. 2 and 3.
the lter-beds employed with the apparatus Referring in l-tllerst place to Fig. l, the apparatus consists of a pressure-proof casing v a, carried by asuitablestand b. A'cov'er c is supplied, secured by means of hinged bolts c', While a dis-k c2 of asbestos provides'a fluid- "tight joint between the lid or cover c and the casing a. Tol'the cov'er c is secured a filterbed d, which consists of a perforated metallic tube. When larger than tw'o inchesin diamstretching process omitted, so that the interstices are reduced in size and at the same time the tensile strength of the cloth bers is The tube d is formed at each endl increased, andthe cloth is thus rendered very suitable as a sti-ainingmatelial. The straining-jacketl is secured to the tube d by means of a cord Wrapped around the grooves d2.
To Iilter the steam, I throw into the bottom of the clean empty casing a a small quantity of porous earth, such as kieselg-uhr or agalite or any other suitable porous land absorbing substance of a likecharacter, sufficient iu A quantity to cover the jacketed cylinder d to the'thickness of from one thirty-second to one-` eighth of an inchl A thicker coating of filtering-earth may be used, but for all ,practical porosity and absorbing powers, but other filtering-earths-such as agalite, chalk, and the So far I have only-provided for the removal ofoily particles, foreign matters in suspension, and moisture of condensation; but when it is desired to remove badsmells from the\'5 steam, due to hydrogen, s-uliid, or to other volatile organic substances, I use about equal proportions of a lterigeartb, such as kieselguhr or agalite, and oxid of zinc or other basic metallic oxid, which is deposited at the bottom of the pressure-'proof casing a, and
before turning on thesteamlcintroduce, v
through the cup f,a fewounces of terebene or other hydrocarbon of thisfY class of terebenes. This has the'evect not only ofpurifying and filtering the steam, but of destroying bad smellsby the chemical and deodorizing action.v
steam and removing oilypar'ticles-andother foreign matter therefrom -it is possible to Thus in addition to filteringl Amo purify steam raised-from canal or othei'niml pure water and use such purifiedv steam `for hnmidifying purposes--suclras in weavingsheds and spinning-rooms.
fied and deodorized has anagreeable aromatic odor, and by its action of developing ozone purilies the atmosphere in such rooms with beneeialresults. During the workingol the apparatus the terebene is'introdnced daily through the cup f, and when required for cleansing `pin-poses thel filter-bed d, attached to the lid,can be removed therewith, so that the cloth strainer' can. be removed and cleansed.
For filtering and deodorizing larger volumes of steam I employ a number of filtering unitsarranged-as shown in Figs. 2 to 4.
I employ any suitable number of filteringcylinders,.according to the volume. of steam to treated, and mount such filtering-cylinders in concentric circles, as shown in the plauvview- Fig. 3, Within avpressure-p'roof cas- `44fing g. The vcylinders deliver thel purified arrangement forsixty-one cylinders.
steam into a receiver `h at the bottom of 'the lcase', from' whence' it passes through the delivery-pipe h. Figs. 2 and 3 show such an A lid or coveri is secured to the casing g by means of swing-belts il', which cover also carries a balance-weight hookj, pressure-gage lc, and
c'up'l. The lter-beds each consist vof a .central perforated drainage-tube fm, screwed and expandedin the diaphragm -plate "n, which forms -a roo-l` to the reservoir or receiver h.
Thepe'r-forated drainagetubes n serve' to carry and support pervious cylinders'o, a concentric circulating-space being provided by distance-pieces p. The pervious cylinders o are wrapped with mercerized uustretched cot- 'ton cloth,` the ends of which are tucked with.- in the cylinders yo and the Whole secured in' `Aposition by meansv of cap-nuts y`p',whieh' screw'.
1 ing a fluid-tight joint..` The'ltering earth or .n
yonthetop of the inner tubes m, s o that the cylinders o are jammed tightly in position,A
the turned-in layers of cotton fabric providwhence it is drawn o by Way of the deliverypipe 7?.,'assh'ow-n by the arrow. 'lerebene may be added when deodorizing the steam through the cup l. To clean the filter-beds,
the cap-nuts p may be unscrewed and the outer cylinders o removed to Wash offv the dirty iltering-earth,or the filter-beds may be washed n Situ by a .reversed vcurrent of clean water delivered through the receiver h,whie h throwsoii the deposit of dirtyltering-earths, the deposit being `removed,'from thecasingfg by Way of the flush-pipe r. to an enlarged scalea portion of the filter-bed. I declare that what I claimis--- 1. The herein-described method of filtering steam consisting in" depositing a 'thineoatg In rig. 4 1 show,
ing of agalite on a suitable bed, and passingthe steam therethrough, vsubstantially as dyescribed. y f ,2.2 The herein-described method of filtering audfdeodorizingsteam consisting in depositvinga mixture of agalite and a basic metallic oXid with an admixture o t'erebeneupon a suitable support, and passing the steam therethrough. v
In Witness whereof I have hereunto set my hand in presence of two Witnesses.
WILLIAM HENRY BARR.
Witnesses:
J osHUAv ENTWISLE, ALFRED YATEs.
US1845400A 1900-05-29 1900-05-29 Method of filtering steam. Expired - Lifetime US666044A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
US1845400A US666044A (en) 1900-05-29 1900-05-29 Method of filtering steam.

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US1845400A US666044A (en) 1900-05-29 1900-05-29 Method of filtering steam.

Publications (1)

Publication Number Publication Date
US666044A true US666044A (en) 1901-01-15

Family

ID=2734600

Family Applications (1)

Application Number Title Priority Date Filing Date
US1845400A Expired - Lifetime US666044A (en) 1900-05-29 1900-05-29 Method of filtering steam.

Country Status (1)

Country Link
US (1) US666044A (en)

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2904184A (en) * 1957-07-01 1959-09-15 Purolator Products Inc Filtering unit
US3037634A (en) * 1958-06-16 1962-06-05 Bowser Inc Water filter
US3256996A (en) * 1960-09-28 1966-06-21 Millipore Filter Corp High pressure filter
US3276186A (en) * 1964-07-22 1966-10-04 Calgon Corp Filter composition and method of removing hydrogen sulfide from water
US4123506A (en) * 1976-08-06 1978-10-31 Deuterium Corporation Utilization of impure steam contaminated with hydrogen sulfide
US4191648A (en) * 1978-02-06 1980-03-04 Kaplan Stephen J Filtration device for filtering temperature controlled fluids
US4192854A (en) * 1976-09-03 1980-03-11 Eic Corporation Process for removing hydrogen sulfide and ammonia from gaseous streams
US4221774A (en) * 1976-08-06 1980-09-09 Deuterium Corporation Isotope enrichment systems

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2904184A (en) * 1957-07-01 1959-09-15 Purolator Products Inc Filtering unit
US3037634A (en) * 1958-06-16 1962-06-05 Bowser Inc Water filter
US3256996A (en) * 1960-09-28 1966-06-21 Millipore Filter Corp High pressure filter
US3276186A (en) * 1964-07-22 1966-10-04 Calgon Corp Filter composition and method of removing hydrogen sulfide from water
US4123506A (en) * 1976-08-06 1978-10-31 Deuterium Corporation Utilization of impure steam contaminated with hydrogen sulfide
US4221774A (en) * 1976-08-06 1980-09-09 Deuterium Corporation Isotope enrichment systems
US4192854A (en) * 1976-09-03 1980-03-11 Eic Corporation Process for removing hydrogen sulfide and ammonia from gaseous streams
US4191648A (en) * 1978-02-06 1980-03-04 Kaplan Stephen J Filtration device for filtering temperature controlled fluids

Similar Documents

Publication Publication Date Title
US3733267A (en) Process of filtration of dry cleaning fluid
US2554748A (en) Water filter
US666044A (en) Method of filtering steam.
US654592A (en) Filtering apparatus.
US590868A (en) Filter
US2952331A (en) Filtering apparatus for exhaust pumps
US651948A (en) Filter.
US609769A (en) Domestic or other filter
US620451A (en) Rudolf helwig
GB1180688A (en) Method and apparatus for the treatment of suspensions
US560261A (en) Filter
US2081353A (en) Filter
GB227707A (en) Improvements in and relating to water softening apparatus
US1195923A (en) Schaft
US2175256A (en) Filter
US3198333A (en) Filter for domestic appliance
US1259498A (en) Filter.
US598391A (en) hiram a
US2096220A (en) Process of cleaning dirty oil
RU194668U1 (en) MULTI-CASSETTE SORPTION FILTER
US139922A (en) Improvement in filters
US1326374A (en) Water-filter.
US634512A (en) Water-filter.
US424679A (en) Ferdinand lascar
US629319A (en) Filtering organ.