US159837A - Improvement in the manufacture of grape-sugar - Google Patents

Improvement in the manufacture of grape-sugar Download PDF

Info

Publication number
US159837A
US159837A US159837DA US159837A US 159837 A US159837 A US 159837A US 159837D A US159837D A US 159837DA US 159837 A US159837 A US 159837A
Authority
US
United States
Prior art keywords
sugar
grape
grain
shaft
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
Publication date
Application granted granted Critical
Publication of US159837A publication Critical patent/US159837A/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Images

Classifications

    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08BPOLYSACCHARIDES; DERIVATIVES THEREOF
    • C08B30/00Preparation of starch, degraded or non-chemically modified starch, amylose, or amylopectin
    • C08B30/12Degraded, destructured or non-chemically modified starch, e.g. mechanically, enzymatically or by irradiation; Bleaching of starch
    • C08B30/18Dextrin, e.g. yellow canari, white dextrin, amylodextrin or maltodextrin; Methods of depolymerisation, e.g. by irradiation or mechanically

Definitions

  • the invention relates to means for effecting the conversion of rice and other grain into a saccharine liquid or glucose or grapesugar solution by one operation, by feeding the grain whole into a vessel, which I call a saccharifier, under steam-pressure, in order completely to effect the conversion of such grain into a saccharine liquid.
  • Glucose sugar is now manufactured from prepared starch, and also from canesugar, but by means which are much more expensive, and involve a longer time, than when, as adopted by me, the raw grain is converted into a saccharine liquid or glucose or grape-sugar solution by one operation. But that the invention may be fully understood I will, by the aid of the accompanying drawings, proceed to describe means pursued by me in carrying the same into effect.
  • Figure 1 represents, by a vertical section, parts of apparatus adapted to carry out my invention.
  • Figs. 2, 3, and 4 represent parts, separately, on a larger scale.
  • a a is a vessel, which I call a saccharifier or digester.
  • This vessel I usually form of wood, and it is adapted to sustain pressure from within of, say, ten to twelve pounds to the square inch. It is formed with a close cover, a, and with an internal step, b, in order that it may sustain the lower end of the hollow shaft or axis a, which at the upper end passes through, while it is guided by, the stuffing-box d in the cover a, and at its upper end this hollow shaft passes into a screw-cap, 0, formed to admit of the shaft revolving freely therein, while it is capable of receiving steam from a suitable steamgenerator through the feedpipe f.
  • the hollow shaft 0 has also applied to it the hollow arms 0, which receive steam from the shaft 0 by means of the pipe 0 and are formed with numerous small holes for the escape of the steam therethrough into the chamber a.
  • On the upper part of this shaft or axis a is applied the beveled-tooth wheel g, the teeth of which are taken into by the teeth of the beveled-tooth wheel h, affixed on the shaft or axis 11, which is supported in suitable bearings, and has motion given to it from a steam-engine or other suitable power.
  • the toothed wheel 1 which, by an intermediate wheel, gives motion to the toothed wheel j affixed on the shaft or axis j, and this shaft j, by the beveled wheels j j thereon, gives motion to the feeding means by which the grain to be treated is supplied to the interior of the vessel a.
  • 70 k are the feeding means, of which there are two shown; but this may be varied, and a description of one of them will serve as a description of the other.
  • each feed-cylinder l is formed with six coi'npartments or feel chambers, l, and each chamber, in the rotatioi of the cylinder l, comes into a position to receive grain supplied from the hopper la, and thence, as it passes round, to deliver it by the open pipe or passage m, through the coverc, to the interior of chamber a.
  • the outer surface of the compartments 1 of the cylinder 1 is formed conical, so that, as any wear takes place between the outer surfaces thereof and the interior of the chamber in which that cylinder revolves, the parts may bepressed closer up and retained in contact 5. but in place thereof the outer surface of the partitions forming the compartments 1 of the cylinder 1 may be parallel, or, properly, cylindrical, when, in order to provide for the wea ing away of the outer surfaces of the partitions in contact with the chamber in which they revolve, these partitions are each formed at those parts with spring-packing.
  • I proceed as follows: I first run dilute acid into the chamber a, the acid solution being generally formed by combining one part of acid with ten of water, or thereabout, and this solution is kept well mixed, as well as heated to a temperature of, say, about 220 Fahrenheit. Steam is supplied to the shaft 0, and thence, through the arms 0 to the chamber a, so as to maintain a temperature in the chamber a of, say, 220 Fahrenheit.
  • a is a pipe, with tap a, capable of being -egulated for the escape of steam from the inverior of the chamber a.
  • o is another pipe, vith tap 0, for drawing off from the chamber l.
  • 1) is a glass gage, communicating in the lsual way, at 12 12, with the top and bottom f the vessel (1, to indicate the height of liquid n that vessel a.
  • a safety-valve (not shown by the drawing) "a employed to regulate the pressure in the hamber a.
  • the acid I find to nswer best for the purpose is dilute sulphuric cid.
  • What I claim is-- 1.
  • the described process of producing saccharine liquid by one operation .in the manufacture of glucose or grape-sugar from whole grain, by feeding such whole grain into a vessel containing sulphuric acid, in successive and regulated quantities, such "essel being supplied with steam by hollow stirrers, performing the double function of stirring and of conveying and distributing the steam.
  • the grain-feeding devices described consisting of the supply reservoir or hopper and the automatic revolving cylinder Z, supplied from the hopper, and provided with a circular series of pockets, and operating to feed intermittently and regularly, in the manner described.

Landscapes

  • Chemical & Material Sciences (AREA)
  • Crystallography & Structural Chemistry (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Biochemistry (AREA)
  • Materials Engineering (AREA)
  • Health & Medical Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Medicinal Chemistry (AREA)
  • Polymers & Plastics (AREA)
  • Organic Chemistry (AREA)
  • Apparatuses For Bulk Treatment Of Fruits And Vegetables And Apparatuses For Preparing Feeds (AREA)

Description

E. E. PEARSE.
Manufacture of Grape Sugar.
No. l59,837. Patented Feb. 16,1875.
HE GRAPHIC (IO- HOTO-UHLSQ &4 PARK PLAOE,M.Y.
UNITED STnTns nTnnT Triton.
EDIVIN EGERTON IEARSE, OF NEW WANDSVVORTH, ASSIGNOR TO THE PATENT GRAPE-SUGAR COMPANY, LIMITED, OF RUPERT STREET, \VHITEOHAPEL, LONDON, ENGLAND.
IMPROVEMENT IN THE MANUFACTURE OF GRAPE-SUGAR.
Specification forming part of Letters Patent No. 1159,837, dated February 16, 1875; application filed February 20, 1874.
To all whom itmay concern:
Be it known that I, EDWIN EGERTON PEARSE, of New Wandsworth, in the county of Surrey, England, have invented certain improvements in the manufacture of glucose or grape-sugar from rice and othen grain, and in apparatus employed therein, of which the following is a specification:
The invention relates to means for effecting the conversion of rice and other grain into a saccharine liquid or glucose or grapesugar solution by one operation, by feeding the grain whole into a vessel, which I call a saccharifier, under steam-pressure, in order completely to effect the conversion of such grain into a saccharine liquid.
Glucose sugar is now manufactured from prepared starch, and also from canesugar, but by means which are much more expensive, and involve a longer time, than when, as adopted by me, the raw grain is converted into a saccharine liquid or glucose or grape-sugar solution by one operation. But that the invention may be fully understood I will, by the aid of the accompanying drawings, proceed to describe means pursued by me in carrying the same into effect.
Figure 1 represents, by a vertical section, parts of apparatus adapted to carry out my invention. Figs. 2, 3, and 4 represent parts, separately, on a larger scale.
In each of the figures the same letters indicate corresponding parts wherever they occur.
a a is a vessel, which I call a saccharifier or digester. This vessel I usually form of wood, and it is adapted to sustain pressure from within of, say, ten to twelve pounds to the square inch. It is formed with a close cover, a, and with an internal step, b, in order that it may sustain the lower end of the hollow shaft or axis a, which at the upper end passes through, while it is guided by, the stuffing-box d in the cover a, and at its upper end this hollow shaft passes into a screw-cap, 0, formed to admit of the shaft revolving freely therein, while it is capable of receiving steam from a suitable steamgenerator through the feedpipe f. The hollow shaft 0 has also applied to it the hollow arms 0, which receive steam from the shaft 0 by means of the pipe 0 and are formed with numerous small holes for the escape of the steam therethrough into the chamber a. On the upper part of this shaft or axis a is applied the beveled-tooth wheel g, the teeth of which are taken into by the teeth of the beveled-tooth wheel h, affixed on the shaft or axis 11, which is supported in suitable bearings, and has motion given to it from a steam-engine or other suitable power. On this shaft i is also applied the toothed wheel 1, which, by an intermediate wheel, gives motion to the toothed wheel j affixed on the shaft or axis j, and this shaft j, by the beveled wheels j j thereon, gives motion to the feeding means by which the grain to be treated is supplied to the interior of the vessel a. 70 k are the feeding means, of which there are two shown; but this may be varied, and a description of one of them will serve as a description of the other. it" is a hopper by which the grain is fed to the feed-cylinder l, which is attached to, and caused to revolve with, the shaft W, as that shaft is caused to revolve by the beveledtooth wheel is being taken into by a beveledtooth wheel, j As shown, each feed-cylinder l is formed with six coi'npartments or feel chambers, l, and each chamber, in the rotatioi of the cylinder l, comes into a position to receive grain supplied from the hopper la, and thence, as it passes round, to deliver it by the open pipe or passage m, through the coverc, to the interior of chamber a. As shown, the outer surface of the compartments 1 of the cylinder 1 is formed conical, so that, as any wear takes place between the outer surfaces thereof and the interior of the chamber in which that cylinder revolves, the parts may bepressed closer up and retained in contact 5. but in place thereof the outer surface of the partitions forming the compartments 1 of the cylinder 1 may be parallel, or, properly, cylindrical, when, in order to provide for the wea ing away of the outer surfaces of the partitions in contact with the chamber in which they revolve, these partitions are each formed at those parts with spring-packing.
In using this apparatus I proceed as follows: I first run dilute acid into the chamber a, the acid solution being generally formed by combining one part of acid with ten of water, or thereabout, and this solution is kept well mixed, as well as heated to a temperature of, say, about 220 Fahrenheit. Steam is supplied to the shaft 0, and thence, through the arms 0 to the chamber a, so as to maintain a temperature in the chamber a of, say, 220 Fahrenheit. This shaft 0 being set in motion, the steam escaping therefrom gradually raises the heat of the acid liquor in the chamber a to 225 Fahrenheit, and to a pressure of, say, :en pounds per square inch, when I gradually tnd slowly commence to feed in the grain to )6 operated upon through one or both of the feed apparatus k, taking care still to maintain zhe temperature of the interior of the vessel a about as stated.
a is a pipe, with tap a, capable of being -egulated for the escape of steam from the inverior of the chamber a. o is another pipe, vith tap 0, for drawing off from the chamber l. 1) is a glass gage, communicating in the lsual way, at 12 12, with the top and bottom f the vessel (1, to indicate the height of liquid n that vessel a. By these means the whole of the grain is ubjected to the action of the steam, which is aused to pass through it, and in a very short ime a complete conversion of it into a sacharine liquid or sugar solution in the 0118,11 er (1. takes place.
A safety-valve (not shown by the drawing) "a employed to regulate the pressure in the hamber a.
In place of wood, metal may be employed DI the vessel a, and a higher pressure may lso be employed 5 but in such case great care necessary, or the sugar produced will be mild to have obtained a burnt flavor.
I form the hollow shaft and the arms thereof f gun-metal, or other metal not injuriously cted upon by the acid. The acid I find to nswer best for the purpose is dilute sulphuric cid.
As the saccharine liquid is run out of the essel a it is acted upon by alkaline solution, s is usual in such cases. I then proceed with what I call the cleansing part of the process that is to say, the separation of the husk and the remaining alkali from the solution.
To facilitate this cleansing, I employ hydraulic-pump apparatus, and force the liquid through suitable filters, the result being a bright and pure saccharine liquid, with very little waste, as compared with the ordinary method of filtration without pressure. The liquid thus obtained is then passed through charcoal filters in the ordinary way, and it is then treated by being acted upon in evaporatin g and vacuum pans in the usual way.
Having thus described my invention, and means which I adopt in carrying the same into effect, I would have it understood that I do not confine myself to the precise details of working as described; but
What I claim is-- 1. The described process of producing saccharine liquid by one operation, .in the manufacture of glucose or grape-sugar from whole grain, by feeding such whole grain into a vessel containing sulphuric acid, in successive and regulated quantities, such "essel being supplied with steam by hollow stirrers, performing the double function of stirring and of conveying and distributing the steam.
2. The combination of the vessel (0, the hollow shaft 0 for the passage, supply, and distribution of the steam, and the feeding devices 70 k Z Z, as shown and described.
3. In combination with an apparatus for producing saccharine liquid from whole grain, the grain-feeding devices described, consisting of the supply reservoir or hopper and the automatic revolving cylinder Z, supplied from the hopper, and provided with a circular series of pockets, and operating to feed intermittently and regularly, in the manner described.
In testimony whereof I have signed my name to this specification in the presence of two subscribing witnesses.
EDWIN EGERTON PEARSE.
Witnesses:
WILLIAM BROOKES, ALFRED GEORGE BROOKES.
US159837D Improvement in the manufacture of grape-sugar Expired - Lifetime US159837A (en)

Publications (1)

Publication Number Publication Date
US159837A true US159837A (en) 1875-02-16

Family

ID=2229247

Family Applications (1)

Application Number Title Priority Date Filing Date
US159837D Expired - Lifetime US159837A (en) Improvement in the manufacture of grape-sugar

Country Status (1)

Country Link
US (1) US159837A (en)

Similar Documents

Publication Publication Date Title
US276990A (en) Manufacture of bicarbonate of soda
US152305A (en) Improvement in refining sugar
US1578221A (en) Clarifier for saccharine solutions
US187881A (en) Alexander manbbe
US243487A (en) Geoege a
US1698505A (en) Chrome tanning material and process of making same
US565669A (en) Apparatus for treating garbage
US247288A (en) Process of manufacturing sugar
US1023257A (en) Starch-conversion process.
US434696A (en) Charlott f
US210339A (en) Improvement in separating and cleaning vegetable fibers for paper-pulp
US137746A (en) Improvement in processes and apparatus for extracting the juices of sugar-cane
US1186655A (en) Process for obtaining fiber from wood and other substances.
US200252A (en) Improvement in apparatus for refining lard
US548424A (en) Augustus d
US275247A (en) Apparatus for preparing mash for fermentation
US628554A (en) Apparatus for sterilizing canned goods.
US576998A (en) Manufacture of glucose or sugar
US268949A (en) Diffusion apparatus
US1311980A (en) Process of making cellulose
US432604A (en) Apparatus for producing bisulphites
US552955A (en) Process of and apparatus for manufacture of sodium bicarbonate
US125112A (en) Improvement in rendering animal matters and drying and pulverizing the same
US789691A (en) Distilling apparatus.
US538577A (en) Apparatus for forming milk of lime