[go: up one dir, main page]

US896551A - Method of cooling soap. - Google Patents

Method of cooling soap. Download PDF

Info

Publication number
US896551A
US896551A US27482305A US1905274823A US896551A US 896551 A US896551 A US 896551A US 27482305 A US27482305 A US 27482305A US 1905274823 A US1905274823 A US 1905274823A US 896551 A US896551 A US 896551A
Authority
US
United States
Prior art keywords
soap
cooling
vacuum
cooled
tube
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
US27482305A
Inventor
Frederic Juergens
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 US27482305A priority Critical patent/US896551A/en
Application granted granted Critical
Publication of US896551A publication Critical patent/US896551A/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Images

Classifications

    • CCHEMISTRY; METALLURGY
    • C11ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
    • C11DDETERGENT COMPOSITIONS; USE OF SINGLE SUBSTANCES AS DETERGENTS; SOAP OR SOAP-MAKING; RESIN SOAPS; RECOVERY OF GLYCEROL
    • C11D13/00Making of soap or soap solutions in general; Apparatus therefor
    • C11D13/02Boiling soap; Refining
    • 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
    • Y10TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10STECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10S159/00Concentrating evaporators
    • Y10S159/14Soap

Definitions

  • the improvement in the method consists of subjecting the hot soap solution during the rocess of cooling to the action of a vacuum.
  • the cooled surfaces of the cooler are constantly swept with Scrapers or the like for the purpose of not only scraping oli any crust of soa which may form from the surfaces, but a so of continuously producing spaces, in vwhich the vacuum can o erate direct upon all the various la ersl of t e lifljuid, before the said spaces are led up with iquid soap.
  • a paratus For carrying out the improved method an a paratus may be used, t e construction of W 'ch is orinstance illustrated in the accomapanying drawing, in which Figure 1 is a view of a complete'a paratus, inclu ding vertical section through the cooler, and Fig. 2 is a horizontal section through the cooler on the line -at of Fig. 1.
  • the cooler consists of a cylindrical jacketed vessel, D, with a conical bottom b, and a central cooling tube E, a cover and an agitator of the followi construction.
  • the central cooling tube E 1s supported on the bottom b. by means of severa egs and is in its upper part reduced in diameter.
  • a sleeve passln a stuffing box of the cover is mounte the upper reduced part of the tube E. It is shown as made in one piece'with a erforated disk, ⁇ from which Iare suspended our external scrapers G and two internal scrapersG.
  • the four external Scrapers G are ada tedto scra e the inside of the interto similar nal wal B, while t e internalscrapers, QQ,
  • the cover is providedwith an inlet A, for the introduction of the hot soap solution from a tank Z, and with an opening, H, connected by a ipe V or the like with an air pump U..
  • The' ottom b of the cooler is normally closed with a slide K and is rovided with an outlet L.
  • a long tube an a short tube are arranged within the reduced upper part of the cooling tube. E, the long tube reaching downto/a point above thev bottom of the cooling tube E and serving for introduction of cold water, while the short tube serves for the discharge of the warmed water.
  • a supply tube (not shown) is attached to the bottom of the'cooler for the introduction of cold waterinto the jacket C between the two walls B and D, and an outlet tube (not shown) andv serves for the dlscharge of the warmed water from the jacket.
  • An opening J is rovided for the introduction of compresse vair by means of ipe T intothe apparatus.
  • i opening M is s own as provide with a safetyvalve rm.
  • Pump U is'operated by means of pulleysl W and X, connected by belt Y.
  • the apparatus is operated as follows: The hot soa solution introduced into the cool r t ough the inlet A, after which the latt r is closed. Cold water is. passed through the jacket or space C between the tube E. The agitator G, F, is put into motion by the dri j' g pulley in such manner that the soap solution 1s stirred up and' ed. At the same time, the air pump U iswithto operation for producing a vacuum in )the cooler through the o enin H. Under thevcombined action of t e cooing water and of the vacuum, the hot soap solutionwill be quicklr' cooled and concentrated.
  • the Scrapers G' constantly sweep the inside of the Wall B and the outside Asolid soap'w 'ch may form, and mix it with mesh with a pinion P, driven ⁇ two Walls B and D,land throu h the cooling is attached to the upper part'of the vessel D,
  • the apparatus can be o erated periodically or continuously. In the latter case the soap mass isintroduced continuously into the apparatus, passes the coolin room ⁇ and leaves 1t at once through the out et L.
  • the obtained solid soap ieces can, in the usual manner, be cut oi, nii'ied and 'com vressed.
  • ⁇ t cooling Water or other medium in the new apparatus is utilized to a very high de ee, which is of s ecial imoitance, seeing, t at the cooling uid is digcult'to obtain in suiiicient quanv tities, more particularly in summer.
  • hitherto known soap coolers consume enor-Y mous quantities of Water.
  • the rapid cooling effected in the new cooler renders it possible to cool largefquantities of hot soap solution in a short time in simple apparatuses of a moderate size.
  • the new method secures to the soap maker a considerably greater independence of the temperatures Without, Whlc'h in summer occasion very great difficulties as is Welly known.
  • the vacuum can be produced equally well in summer and in winter andindependently of the cooling medium at hand.
  • the new method renders it possible to avoid all the lcrystallizationsl of soap on the latter becoming torpid and also the inconvenient granulations and other irregularities which are so frequently thereby produced in the old methods.
  • the method of cooling soap which consists incooling hot soap solution in a closed cooled vessel, subjecting the soap solution during cooling to the action of a vacuum, and' scraping oi any crust of soap which may form on the cooled surfaces.
  • the method of cooling soap which consists in cooling hot soap solution in a closed cooled vessel, and subjecting the solution during coolin to the action of a vacuum.

Landscapes

  • Chemical & Material Sciences (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Wood Science & Technology (AREA)
  • Organic Chemistry (AREA)
  • Detergent Compositions (AREA)

Description

110.996,551. PATBNTED A11-(1.191909. 1'. JRGENS.
METHOD OF COOLING SOAP. APPLIOATION FILED 11119.19, 1905.
` INvENTQR, W\TNESSES FREDEmc-JURGENS.,
` all crystallization through j to turn on FREDERIC JRGENS, OF SANGERHAUSEN, GERMANY.V
lmTHOD OF C pecication of Letters Patent. Application mea August 19, 1905. serial No. 274,823.
ooLING son?.
Patented Aug. 18, 1908.
' method of cooling soap, whereby the cooling and the concentration of the hot soap solution is accelerated and solid soap is separated in a smooth and amorphous condition, while and the thereby-produced granulation, and the mottled, grained or cloudy appearance (known as curling) of the soap, is avoided.
The improvement in the method consists of subjecting the hot soap solution during the rocess of cooling to the action of a vacuum. n order that also the lower layers of solution, which are subjected to the pressure of the head of the liquid, may be exposed to theaction of the/vacuum, the cooled surfaces of the cooler are constantly swept with Scrapers or the like for the purpose of not only scraping oli any crust of soa which may form from the surfaces, but a so of continuously producing spaces, in vwhich the vacuum can o erate direct upon all the various la ersl of t e lifljuid, before the said spaces are led up with iquid soap. For carrying out the improved method an a paratus may be used, t e construction of W 'ch is orinstance illustrated in the accomapanying drawing, in which Figure 1 is a view of a complete'a paratus, inclu ding vertical section through the cooler, and Fig. 2 is a horizontal section through the cooler on the line -at of Fig. 1.
Similar letters of reference refer parts in both views. Y The cooler consists of a cylindrical jacketed vessel, D, with a conical bottom b, and a central cooling tube E, a cover and an agitator of the followi construction. The central cooling tube E 1s supported on the bottom b. by means of severa egs and is in its upper part reduced in diameter. A sleeve passln a stuffing box of the cover is mounte the upper reduced part of the tube E. It is shown as made in one piece'with a erforated disk, `from which Iare suspended our external scrapers G and two internal scrapersG. The four external Scrapers G, are ada tedto scra e the inside of the interto similar nal wal B, while t e internalscrapers, QQ,
Hserve for scraping the outside of the cooling tube E. All six scrape'rs are connected with each other and st'fened by means cfa helically'bent plate F and a cross piece, which latter is mounted to turn on the oWer end of the reduced part or' the cooling tube E. At the top end of the sleeve is fastened a large bevel wheel yS, in from a pulleyQ, to rotate the inside Scrapers and the screw in one direction, While the outside scrapers are driven in the opposite direction by engagement of pinion with bevel wheel R. The cover is providedwith an inlet A, for the introduction of the hot soap solution from a tank Z, and with an opening, H, connected by a ipe V or the like with an air pump U.. The' ottom b of the cooler is normally closed with a slide K and is rovided with an outlet L. A long tube an a short tube are arranged within the reduced upper part of the cooling tube. E, the long tube reaching downto/a point above thev bottom of the cooling tube E and serving for introduction of cold water, while the short tube serves for the discharge of the warmed water. A supply tube (not shown) is attached to the bottom of the'cooler for the introduction of cold waterinto the jacket C between the two walls B and D, and an outlet tube (not shown) andv serves for the dlscharge of the warmed water from the jacket. .An opening J is rovided for the introduction of compresse vair by means of ipe T intothe apparatus.,- i opening M is s own as provide with a safetyvalve rm. Pump U is'operated by means of pulleysl W and X, connected by belt Y.
The apparatus is operated as follows: The hot soa solution introduced into the cool r t ough the inlet A, after which the latt r is closed. Cold water is. passed through the jacket or space C between the tube E. The agitator G, F, is put into motion by the dri j' g pulley in such manner that the soap solution 1s stirred up and' ed. At the same time, the air pump U is putinto operation for producing a vacuum in )the cooler through the o enin H. Under thevcombined action of t e cooing water and of the vacuum, the hot soap solutionwill be quicklr' cooled and concentrated. The Scrapers G', constantly sweep the inside of the Wall B and the outside Asolid soap'w 'ch may form, and mix it with mesh with a pinion P, driven `two Walls B and D,land throu h the cooling is attached to the upper part'of the vessel D,
lifted, and' thus well I -of the coolinltubeE, scrape off any crust of l the liquid soap. 'Besides this, they constantly produce, during their rotation, spaces through which the vacuum can act upon all the several layers and particles of the solution. When the solution is sufiiciently cooled and has attained the proper consistency, the port H connected with the vacuum-pump is' closed, and the port J is opened, removing the vacuum so that the compressed air entering through this opening causes a sudden solidiiication or con ealin of the soap and forces the same in the esire form through the outlet L, as soon as the slide K is Withdrawn. By reason of the extremely quick solidiying of/the soap, the formation of crystals is prevented, since crystals re uire a considerable time for formation, an cannot be produced in a liquid which suddenly solidifls.
The apparatus can be o erated periodically or continuously. In the latter case the soap mass isintroduced continuously into the apparatus, passes the coolin room` and leaves 1t at once through the out et L. The obtained solid soap ieces can, in the usual manner, be cut oi, nii'ied and 'com vressed.
With theaid of `the vacuum, `t cooling Water or other medium in the new apparatus is utilized to a very high de ee, which is of s ecial imoitance, seeing, t at the cooling uid is digcult'to obtain in suiiicient quanv tities, more particularly in summer. The
hitherto known soap coolers consume enor-Y mous quantities of Water. The rapid cooling effected in the new cooler renders it possible to cool largefquantities of hot soap solution in a short time in simple apparatuses of a moderate size.
The new method secures to the soap maker a considerably greater independence of the temperatures Without, Whlc'h in summer occasion very great difficulties as is Welly known. The vacuum can be produced equally well in summer and in winter andindependently of the cooling medium at hand. At last the new method renders it possible to avoid all the lcrystallizationsl of soap on the latter becoming torpid and also the inconvenient granulations and other irregularities which are so frequently thereby produced in the old methods.
sists in cooling hot soap so ution in a closedff cooled vessel, subjecting the soap solution during cooling to agitation and to the action of a vacuum, and scraping off any crust of soap which may form on the'cooled surfaces.
2. The method of cooling soap, which consists incooling hot soap solution in a closed cooled vessel, subjecting the soap solution during cooling to the action of a vacuum, and' scraping oi any crust of soap which may form on the cooled surfaces.
3. The method of cooling soap, which consists in cooling hot soap solution in a closed vessel having cooled Walls and a cooled internal 'bod ,A subjecting the soap solution lduring coo lng,' to the action of a vacuum,
and scraping oi any crust of soap which may form on the cooled walls or cooled internal body.
4. The method of cooling soap, which consists in cooling hot soap solution in a closed cooled vessel, and subjecting the solution during coolin to the action of a vacuum.
' 5. The met od of coolin soap, which consists in cooling hot soap so ution in a closed cooled vessel While sub'ected to the action of a vacuum and suddenly removing the vacuum.
6. The method of cooling soap, which'consists in a itating hot soap solution in a closed coo ed vessel while subjected to the action of a vacuum and scrapin of any crust of soa which may form on t e cooled surfaces, and suddenly removing the vacuum. In testimony whereof, I have signed my name to this specification in the presence of two subscribing witnesses, this eighth day of August 1905.
. 1 FREDERIC JRGENS. Witnesses AUGUST GERM,
CARL TJEHmsWrrz.
US27482305A 1905-08-19 1905-08-19 Method of cooling soap. Expired - Lifetime US896551A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
US27482305A US896551A (en) 1905-08-19 1905-08-19 Method of cooling soap.

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US27482305A US896551A (en) 1905-08-19 1905-08-19 Method of cooling soap.

Publications (1)

Publication Number Publication Date
US896551A true US896551A (en) 1908-08-18

Family

ID=2964978

Family Applications (1)

Application Number Title Priority Date Filing Date
US27482305A Expired - Lifetime US896551A (en) 1905-08-19 1905-08-19 Method of cooling soap.

Country Status (1)

Country Link
US (1) US896551A (en)

Cited By (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2544162A (en) * 1947-12-22 1951-03-06 William C Newman Freezer
US2991161A (en) * 1959-11-23 1961-07-04 Autoclave Eng Inc Autoclave
US3054729A (en) * 1958-11-28 1962-09-18 Arthur F Smith Distillation film wiping apparatus
US3101598A (en) * 1959-06-24 1963-08-27 Anthony J Ross Method and apparatus for freezing liquids
US3238739A (en) * 1959-04-27 1966-03-08 Anthony J Ross Auger type ice maker
US3290895A (en) * 1959-02-18 1966-12-13 Ross Temp Inc Apparatus for making flake ice
US4778277A (en) * 1984-08-09 1988-10-18 Kraftwerk Union Aktiengesellschaft Mixing device
US5233916A (en) * 1992-07-13 1993-08-10 Robert L. Butler Apparatus for cooking grits and hot cereal mixtures
US6058828A (en) * 1998-06-30 2000-05-09 Food Industry Research And Development Institute Continuous cooking system for solid daily dishes
US6167798B1 (en) * 2000-04-19 2001-01-02 General Mills, Inc. Cooker die and rotary cutter removably securing mechanism
US6189439B1 (en) 2000-05-25 2001-02-20 General Mills, Inc. Cooker die and rotary cutter removably securing mechanism
US6767198B2 (en) 2001-10-17 2004-07-27 General Mills, Inc. Rotary cutter assembly

Cited By (14)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2544162A (en) * 1947-12-22 1951-03-06 William C Newman Freezer
US3054729A (en) * 1958-11-28 1962-09-18 Arthur F Smith Distillation film wiping apparatus
US3290895A (en) * 1959-02-18 1966-12-13 Ross Temp Inc Apparatus for making flake ice
US3238739A (en) * 1959-04-27 1966-03-08 Anthony J Ross Auger type ice maker
US3101598A (en) * 1959-06-24 1963-08-27 Anthony J Ross Method and apparatus for freezing liquids
US2991161A (en) * 1959-11-23 1961-07-04 Autoclave Eng Inc Autoclave
US4778277A (en) * 1984-08-09 1988-10-18 Kraftwerk Union Aktiengesellschaft Mixing device
US5233916A (en) * 1992-07-13 1993-08-10 Robert L. Butler Apparatus for cooking grits and hot cereal mixtures
US6058828A (en) * 1998-06-30 2000-05-09 Food Industry Research And Development Institute Continuous cooking system for solid daily dishes
US6167798B1 (en) * 2000-04-19 2001-01-02 General Mills, Inc. Cooker die and rotary cutter removably securing mechanism
US6189439B1 (en) 2000-05-25 2001-02-20 General Mills, Inc. Cooker die and rotary cutter removably securing mechanism
US6767198B2 (en) 2001-10-17 2004-07-27 General Mills, Inc. Rotary cutter assembly
US20050009653A1 (en) * 2001-10-17 2005-01-13 Weinstein James N. Rotary cutter assembly
US7094169B2 (en) 2001-10-17 2006-08-22 General Mills, Inc. Rotary cutter assembly

Similar Documents

Publication Publication Date Title
US896551A (en) Method of cooling soap.
US2983652A (en) Fermenter
CN106901100A (en) Freeze concentration purifying plant
CN105129852B (en) The system that a kind of high-efficiency self-circulation wet method continuously prepares sodium dichromate
CN108435045A (en) A kind of concrete steel structural anticorrosion coating producing process
CN116271889B (en) A food additive production dryer
CN206980552U (en) A kind of banksia rose perfumed soap producing device
CN2724801Y (en) Ultrasonic continuous flowing and counter-flowing extracting equipment
CN209655716U (en) A kind of spherical drying machine with cleaning function
CN116251377B (en) Potassium chloride evaporation crystallization device
CN206355982U (en) A kind of cooling water circulation highly effective reaction kettle
CN209291973U (en) A kind of spheric active carbon production equipment
CN207324818U (en) A kind of carburizing reagent device of nano-calcium carbonate production
CN206082496U (en) But recovery type methyl chloroformate apparatus for producing
CN207347543U (en) A kind of intelligence mature vinegar production equipment
CN205868237U (en) Energy -efficient sludge water pyrolytic reaction equipment
CN215985412U (en) Biomacromolecule medicine extraction element that awaits measuring
CN214051313U (en) Liquid tank is used in foam extinguishing agent production
CN206428217U (en) A kind of lemon extraction element
CN209307195U (en) A kind of sludge smashing drying device
CN218372112U (en) Calcium superphosphate slurry mixing, stirring and curing production equipment
US583751A (en) John william henry james
CN220214832U (en) High tower granulator
CN109569459B (en) Separate bin type reaction furnace suitable for salting-out method
CN205893196U (en) High -efficient circulating flat turn type leaching device