US250362A - Peters - Google Patents
Peters Download PDFInfo
- Publication number
- US250362A US250362A US250362DA US250362A US 250362 A US250362 A US 250362A US 250362D A US250362D A US 250362DA US 250362 A US250362 A US 250362A
- Authority
- US
- United States
- Prior art keywords
- starch
- liquor
- settling
- trough
- tanks
- 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
Links
- 229920002472 Starch Polymers 0.000 description 48
- 239000008107 starch Substances 0.000 description 48
- 235000019698 starch Nutrition 0.000 description 38
- 239000007788 liquid Substances 0.000 description 10
- 238000000151 deposition Methods 0.000 description 4
- 230000000153 supplemental Effects 0.000 description 4
- 230000000694 effects Effects 0.000 description 2
- 230000002349 favourable Effects 0.000 description 2
- 230000005484 gravity Effects 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 238000005086 pumping Methods 0.000 description 2
- 238000003756 stirring Methods 0.000 description 2
Images
Classifications
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08B—POLYSACCHARIDES; DERIVATIVES THEREOF
- C08B30/00—Preparation of starch, degraded or non-chemically modified starch, amylose, or amylopectin
- C08B30/04—Extraction or purification
- C08B30/042—Extraction or purification from cereals or grains
- C08B30/044—Extraction or purification from cereals or grains from corn or maize
Definitions
- the raw starch-liquor having a density of, say, 5 Baum
- table or a succession of tables, upon the bottom of which the starch is deposited.
- the greater portion of the starch is deposited upon the first thirty or forty feet of the table; but in order to secure all the starch it is customary to employ tables of great length, in some cases one hundred and twenty-five or even one hundred and fifty feet in length, or to run the starch-liquor over a series of tables of shorter length.
- the starchliquor In running a distance of sixty feet over a table the starchliquor is lowered in density from, say, 5 Baume to, say, 1 Baum, and the starch deposited on the lower portion of the table is always less pure than that deposited upon the higher portion of it.
- I preferably provide each table with two settling-tanks, which are filled alternately by the overflowing starch-liquor, and the table can thus be continuously employed under the most favorable conditions for obtaining the purest deposit of starch.
- Figure 1 is a top view
- Fig. 2 is a longitudinal vertical section, of the apparatus.
- the trough A is constructed in the usual manner, and for the purpose of illustrating my invention may be assumed to be sixty feet in length.
- the raw-starch liquor is introduced at the upper end, B, into the trough, and as it flows through the trough deposits upon the bottom thereof, say, eighty per cent. of the starch which it originally contained. Assuming it to have had a density of 5 Baum when first introduced into the upper end of the starch-trough, the liquid overflowing from the opposite end 0 will therefore have a density of, say, 1 Baum.
- This liquid is discharged from the lower end, 0, of the trough upon a chute, D, by which it is conducted either to the settling-tank E or the settling-tank F, as may be required.
- the feedingot' the raw-starch liquor is arrested, and the deposited starch is removed from the trough and the feeding of raw-starch liquor recom men ced.
- the chute is arranged to conduct the overflowing starch-liquor to the other settling-tank.
- the settling-tanks are made of sufficieut capacity to hold the quantity of starch overflowing from the lower end of the trough during the operation of depositing a charge of starch upon the bottom of the trough.
- the necessity of pumping from the settlingtanks may be avoided by providing the supplemental table G, arranged on a lower level than the bottom of the settling-tanks, so that the concentrated liquid maybe run by its own gravity from the settling-tanks, respectively, through one-0f the pipes g to the upper end. of the supplemental table G.
- the herein-described method of separating starch from raw-starch liquor which consists in first running the raw liquor over a comparatively short starch-table, and in collecting and concentrating the overflow therefrom, and
- the starch-table A in combination with a settling-tank arranged to receive the overflow from the table A? and provided with a stirrer, and means for reconducting the lower stratum of its contents to astarchtable, substantially as and for the purpose set forth.
Landscapes
- Chemical & Material Sciences (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)
- Polysaccharides And Polysaccharide Derivatives (AREA)
Description
(No Model.)
H. O.HU1V[PHREY.
METHOD OF SETTLING STARGH LI UOR. No. 250,362. Patented Dec. 6,1881.
NVENTOR.
UNITED STATES PATENT OFFICE.
HENRY G. HUMPHREY, ()F NE\V YORK, N. Y.
METHOD OF SETTLING STARCH-LIQUOR.
SPECIFICATION forming part of Letters Patent No. 250,362, dated December 6, 1881.
Application filed September 22, 1881. (No model.)
To all whom it may concern:
Be it known that I, HENRY O. HUMPHREY, of the city and State of New York, have invented an Improved Method of Settling Starch- Liquor, of which the following is a specification.
In the ordinary method of manufacturing starch, the raw starch-liquor, having a density of, say, 5 Baum, is run over a long trough or so-called table, or a succession of tables, upon the bottom of which the starch is deposited. By far the greater portion of the starch is deposited upon the first thirty or forty feet of the table; but in order to secure all the starch it is customary to employ tables of great length, in some cases one hundred and twenty-five or even one hundred and fifty feet in length, or to run the starch-liquor over a series of tables of shorter length. In running a distance of sixty feet over a table the starchliquor is lowered in density from, say, 5 Baume to, say, 1 Baum, and the starch deposited on the lower portion of the table is always less pure than that deposited upon the higher portion of it.
It is the threefold object of my invention to dispense with the necessity for the use of long tables, and also to increase the purity of the starch deposit, and to shorten the operation of depositing the starch. To thateud Iemploy, in combination with acomparatively short starchtable, one or more settling-tanks, into which the overflow from the starch-tableis d ischarged, and which, when full, I allow to stand for six hours, more or less, until the heavier materials have settled into the lower stratum of the liquid contained in the tanks. 1 then draw off the clear liquor, and thus have remaining a liquor containing sufficient starch to give it a density of, say, 4 or 5 Baum, which I then stir up and run over the table. I preferably provide each table with two settling-tanks, which are filled alternately by the overflowing starch-liquor, and the table can thus be continuously employed under the most favorable conditions for obtaining the purest deposit of starch. By the use of several settling-tanks ample time is allowed for the concentration of the raw starch-liquor previously to running it a second time over the starch-table.
The apparatus required to carry out my method of collecting the starch is of simple and well-known character, as will be seen from the accompanying drawings, which represent two starch-troughs provided with two settlingtanks.
In these drawings, Figure 1 is a top view, and Fig. 2 is a longitudinal vertical section, of the apparatus.
The trough A is constructed in the usual manner, and for the purpose of illustrating my invention may be assumed to be sixty feet in length. The raw-starch liquor is introduced at the upper end, B, into the trough, and as it flows through the trough deposits upon the bottom thereof, say, eighty per cent. of the starch which it originally contained. Assuming it to have had a density of 5 Baum when first introduced into the upper end of the starch-trough, the liquid overflowing from the opposite end 0 will therefore have a density of, say, 1 Baum. This liquid is discharged from the lower end, 0, of the trough upon a chute, D, by which it is conducted either to the settling-tank E or the settling-tank F, as may be required. As often as there is a sufficient deposit of starch in the settling-trough the feedingot' the raw-starch liquor is arrested, and the deposited starch is removed from the trough and the feeding of raw-starch liquor recom men ced. When one of the settling-tanks is full the chute is arranged to conduct the overflowing starch-liquor to the other settling-tank. The settling-tanks are made of sufficieut capacity to hold the quantity of starch overflowing from the lower end of the trough during the operation of depositing a charge of starch upon the bottom of the trough. After standing six hours, more or less, in the settling-tank, the superincumbent clear liquor is drawn off therefrom through the pipes c and f, respectively, which in the drawings are represented as being so placed as to effect the discharge of four-fifths of the contents of either tank. The remaining liquid in the tank, on being stirred by means of the stirrer E, is brought to a uniform density, which will be found to he, say, 5Baum. Havingbeen thusstirred,itisdrawn or pumped from the tank and discharged upon the starch table, where, by reason of its concentration, the starch it contains is deposited with the usual rapidity.
The necessity of pumping from the settlingtanks may be avoided by providing the supplemental table G, arranged on a lower level than the bottom of the settling-tanks, so that the concentrated liquid maybe run by its own gravity from the settling-tanks, respectively, through one-0f the pipes g to the upper end. of the supplemental table G.
I claim as my invention- 1. The herein-described method of separating starch from raw-starch liquor, which consists in first running the raw liquor over a comparatively short starch-table, and in collecting and concentrating the overflow therefrom, and
in then running such concentrated liquor again over a table.
2. In apparatus for separating starch from raw-starch liquor, the starch-table A, in combination with a settling-tank arranged to receive the overflow from the table A? and provided with a stirrer, and means for reconducting the lower stratum of its contents to astarchtable, substantially as and for the purpose set forth.
H. O. HUMPHREY.
Witnesses:
H. E. NIEsE, R0131. MOELLER.
Publications (1)
Publication Number | Publication Date |
---|---|
US250362A true US250362A (en) | 1881-12-06 |
Family
ID=2319671
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
US250362D Expired - Lifetime US250362A (en) | Peters |
Country Status (1)
Country | Link |
---|---|
US (1) | US250362A (en) |
-
0
- US US250362D patent/US250362A/en not_active Expired - Lifetime
Similar Documents
Publication | Publication Date | Title |
---|---|---|
US250362A (en) | Peters | |
US1076666A (en) | Apparatus for thickening and agitating pulp. | |
US2124284A (en) | Separation of starch from gluten | |
US2233641A (en) | Pulp treatment | |
US2239604A (en) | Sedimentation apparatus | |
US708494A (en) | Apparatus for extracting metals from ores. | |
US1983805A (en) | Gas agitated crystallizing and curing tank | |
US2022093A (en) | Process for the recovery of nonsugars from saccharine materials | |
US1211828A (en) | Apparatus for thickening and agitating pulp. | |
NO132192B (en) | ||
US2624657A (en) | Submerged blast reaction tank | |
US289979A (en) | Apparatus for extracting gluten from the waste water of starch-works | |
US1385701A (en) | Process of recovering valuable solution from mixtures | |
US838717A (en) | Process of electroplating. | |
US1345034A (en) | Recovery of solubles from flue-dust | |
US552955A (en) | Process of and apparatus for manufacture of sodium bicarbonate | |
US958272A (en) | Process of separating liquids from solids. | |
US508915A (en) | Wabhinqton | |
US552895A (en) | Process of and apparatus for making carbonates of soda | |
US894417A (en) | Treating comminuted solids with liquids. | |
US694138A (en) | Process of manufacturing white lead. | |
US986541A (en) | Manufacture of starch. | |
US636750A (en) | Apparatus for galvanizing. | |
US1374370A (en) | Electrochemical gold-separator | |
US1067890A (en) | Process of clarifying raw sugar. |