US588521A - Apparatus for defecating saccharine juices - Google Patents
Apparatus for defecating saccharine juices Download PDFInfo
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- US588521A US588521A US588521DA US588521A US 588521 A US588521 A US 588521A US 588521D A US588521D A US 588521DA US 588521 A US588521 A US 588521A
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- fermentation
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- CVHZOJJKTDOEJC-UHFFFAOYSA-N Saccharin Chemical compound C1=CC=C2C(=O)NS(=O)(=O)C2=C1 CVHZOJJKTDOEJC-UHFFFAOYSA-N 0.000 title description 6
- 238000000855 fermentation Methods 0.000 description 28
- 230000004151 fermentation Effects 0.000 description 26
- 238000000034 method Methods 0.000 description 24
- 238000001556 precipitation Methods 0.000 description 24
- 238000005352 clarification Methods 0.000 description 18
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 16
- 239000012530 fluid Substances 0.000 description 14
- 239000002245 particle Substances 0.000 description 14
- 238000001816 cooling Methods 0.000 description 12
- 239000012535 impurity Substances 0.000 description 12
- 238000000926 separation method Methods 0.000 description 8
- 241000005139 Lycium andersonii Species 0.000 description 6
- 238000004140 cleaning Methods 0.000 description 6
- 230000000694 effects Effects 0.000 description 6
- 239000003153 chemical reaction reagent Substances 0.000 description 4
- 230000001066 destructive Effects 0.000 description 4
- 239000007788 liquid Substances 0.000 description 4
- 238000004321 preservation Methods 0.000 description 4
- 238000004062 sedimentation Methods 0.000 description 4
- 239000000725 suspension Substances 0.000 description 4
- 235000013311 vegetables Nutrition 0.000 description 4
- 235000008733 Citrus aurantifolia Nutrition 0.000 description 2
- CZMRCDWAGMRECN-UGDNZRGBSA-N D-sucrose Chemical compound O[C@H]1[C@H](O)[C@@H](CO)O[C@@]1(CO)O[C@@H]1[C@H](O)[C@@H](O)[C@H](O)[C@@H](CO)O1 CZMRCDWAGMRECN-UGDNZRGBSA-N 0.000 description 2
- 235000004789 Rosa xanthina Nutrition 0.000 description 2
- 241000109329 Rosa xanthina Species 0.000 description 2
- 229940081974 Saccharin Drugs 0.000 description 2
- 229960004793 Sucrose Drugs 0.000 description 2
- 235000015450 Tilia cordata Nutrition 0.000 description 2
- 235000011941 Tilia x europaea Nutrition 0.000 description 2
- 238000003831 Wilkinson decarbonylation reaction Methods 0.000 description 2
- 244000052616 bacterial pathogens Species 0.000 description 2
- 230000015572 biosynthetic process Effects 0.000 description 2
- 238000007664 blowing Methods 0.000 description 2
- 238000009835 boiling Methods 0.000 description 2
- 239000003795 chemical substances by application Substances 0.000 description 2
- 235000009508 confectionery Nutrition 0.000 description 2
- 230000013872 defecation Effects 0.000 description 2
- 238000007599 discharging Methods 0.000 description 2
- 235000013399 edible fruits Nutrition 0.000 description 2
- 230000002349 favourable Effects 0.000 description 2
- 238000005755 formation reaction Methods 0.000 description 2
- 230000014509 gene expression Effects 0.000 description 2
- 239000004571 lime Substances 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 235000013372 meat Nutrition 0.000 description 2
- 230000000414 obstructive Effects 0.000 description 2
- 230000003449 preventive Effects 0.000 description 2
- 230000002035 prolonged Effects 0.000 description 2
- 102000004169 proteins and genes Human genes 0.000 description 2
- 108090000623 proteins and genes Proteins 0.000 description 2
- 235000019204 saccharin Nutrition 0.000 description 2
- 239000000901 saccharin and its Na,K and Ca salt Substances 0.000 description 2
- 239000007787 solid Substances 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- 230000001131 transforming Effects 0.000 description 2
Images
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
- F28F19/00—Preventing the formation of deposits or corrosion, e.g. by using filters or scrapers
- F28F19/01—Preventing the formation of deposits or corrosion, e.g. by using filters or scrapers by using means for separating solid materials from heat-exchange fluids, e.g. filters
Definitions
- My invention relates to improvements in apparatus for the defecation of cane-juice; and it consists of certain novel features hereinafter described and claimed.
- the quality of sugar is largely determined by the clarification of the cane-juice.
- the sedimentation in open vessels presents the serious objection that exposure of the juice to the air subjects it to the danger of molecular changes through fermentation, this increasing in degree as the exposure is prolonged. It is safe to afiirm that no juice can be allowed to remain a sufficient length of time in open vessels for proper precipitation without serious loss (through molecular changes) in quantity and quality of sugar. Cane-juice as run from the clarifiers and left in the open settling-tanks is in a most favorable condition for-fermentation.
- Fermentation is slow to take place below Fahrenheit and is arrested at a temperature somewhat below the boiling-point. It is most favored between and 100.
- the mechanism best adapted to the clarification of juice in closed vessels may present itself in different forms to different persons, but I have shown one form of a pparatus which I believe suitable for this purgose.
- Figure l represents the apparatus in elevation. Many of the non-essential elements are omitted and the apparatus is shown diagrammatically.
- Fig. 2 represents a central in any convenient way, and in which the lime or other chemical reagents are added to the juice before it is carried over to the elarifiers. There should be enough of these tanks A to allow them to be frequently washed out, so that fermentation may be as far as possible avoided before the juice gets to the clarifiers.
- the juice is pumped from these tanks A through the branch pipes b and the main pipe B to the pump 0, whence it is delivered through the pipe D and the branches d to the clarifiers E.
- These various main and branch pipes are provided with valves wherever required, and so, in fact, are all the pipes in the system, and it will not be necessary to refer to these valves specifically.
- the clarifiers E are preferably made of a cylindrical shell E with spherical bottom E and dome-shaped top E and both top and bottom are secured to the cylindrical shell, so as to make a steam-tight joint, as by bolts 6, or in any other convenient way.
- the top E is made detachable for purposes of occasional cleaning out, and is preferably provided with an eyebolt e, to which a tackle can be hooked, whereby the top may be conveniently lifted off after the bolts 0 are unscrewed.
- This top or cap E is also preferably provided with a valve-seat c for the safety-valve Q, but this valve-may be connected to the shell E or attached to the clarifier in any convenient way.
- the heated juice is drawn from the clarifierthrough the branch pipesfand the pipes F into the pipe G, whence it is delivered through the pipes g to the tanks II, from which tanks the clarified juice is pumped to the vacuum pans or other concentrating apparatus. (Not shown.)
- the settlings in the bottoms E are drawn off through the pipes 70 into the pipe K, whence they are delivered through the pipes it into the tanks L.
- the clearer portion of the liquid in the tanks L is drawn off through the pipe M, while the more turgid portions are drained through the pipes 77 and the main pipe N to the filter-press P, which is operated in the usual well-known way.
- the juice in the elarifiers is heated by a steam-pipe, preferably in the form of a coil R, the steam being fed in through the pipes r and controlled by the valve r, while the condensed water from this coil R either escapes, as at r", or is led to the hot-well by any suitable pipe. (Not shown.) Any other arrangement of heating-pipes may be adopted, if preferred.
- Sight-tubes S are preferably provided on each clarifier, but these are not absolutely necessary. In practice it would be preferable to have a sufficient number of the clarifiers to allow the heated juice to cool slowly and to settle gradually, but if it be desired to expedite the process of cooling a waterjacket T, inclosing each clarifier or a part thereof, may be added to the apparatus, if desired. Thus I have shown such a waterjacket, which is illustrated in detail in Fig. 2, the cold water being fed in through the pipe and. escaping through the pipe i, but this water-jacket would not ordinarily be necessary.
- I provide a wash-out pipe W for water and a steam-pipe V for injecting steam into the clarifier after the juice has been withdrawn therefrom.
- the same may be either provided with roses or they may be provided with orifices set at an angle to the inner surface of the cylindrical shell, whereby a spiral or vertical direction may be given to the steam or Water, and thus the various parts of the interior of the shell may be more thoroughly cleansed than were these jets to be projected directly in toward the center of the clarifier.
- These steam and water pipes should also preferably be so arranged that a hose may be coupled onto the same when the top E is removed, and thus each and every part of the interior of the clarifier may be reached by the steam or water, or both.
- the clarifier In the operation of the device the clarifier is filled with juice very nearly to the top of the cylindrical portion, and then steam is turned on to the heating-coil R. The heat is continued until a pressure of about fifteen pounds above that of the atmosphere is attained on the inside of the clarifier, at which pressure the temperature of the liquidsis about 240 Fahrenheit, prior to which time all of the albumen will have been coagulated. This pressure may be noted either from an ordinary pressure-gage (not shown) attached to the clarifier, or from the blowing off of the safety-valve Q. After the heatedjuice has remained long enough to cool and V settle sufficiently the clearer portions are drawn off through the pipes f, while the scum and sediment are drawn off through the pipe 715, as has been hereinbefore described.
- each clarifier' After discharging, each clarifier'should be either washed out through the steam and water pipes already mentioned, or the tops may be periodically removed and the clariffer thoroughly cleaned out.
- connection-currents are not violent and the solid particles are not broken up so fine as to fail to be readily precipitated during the process of cooling.
- a closed vessel adapted to withstand internal pressure, a pump and pipes for supplying juice to said vessel, a steamcoil mounted in said vessel near the base thereof and adapted to heat said juice from contact with the exterior of said steam-coil,
- a closed vessel adapted to withstand internal pressure, a pump and pipes for supplying juice to said vessel, a steamcoil mounted in said vessel near the base thereof and adapted to heat said juice from contact with the exterior of said steam-coil, pipes opening into the said vessel near the base thereof for drawing off the clearer portion of the juice after it has settled, and a separate pipe opening into the base of said vessel for drawing off the sediment, and a jacket inclosing the sides of said vessel,with means for injecting fluid into said jacket for cooling the contents of said vessel, substantially as described.
- a closed vessel provided with a steam-tight top entirely removable, and a safety-valve, a pump and pipes for supplying juice to said vessel and for drawing off the juice therefrom when desired, and a steamcoil mounted in the said vessel near the base thereof and an opening through the sides of said vessel, and adapted to heat the juice by contact with the exterior of said coil, and a jacket inclosing the sides of said vessel,with means for injecting fluid into said jacket for cooling the contents of said vessel, substantially as described.
- a closed vessel with a steamtight top wholly removable, and a curved bottom a pump and pipes for supplying juice to said vessel, a steam-coil mounted in said vessel near the base thereof and adapted to heat IIO the juice from contact with the exterior of said coil, pipes mounted in the sides of said Vessel near the base thereof for drawing off the clearer portion of the juice after it has settled, and a separate pipe connected to the lower portion of the curved bottom and adapted to draw off the sediment from the said Vessel, and a jacket inclosing the sides of said vessehwith means for in jecting fluid into the said jacket for cooling the contents of said 10 vessel, substantially as described.
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- Beans For Foods Or Fodder (AREA)
Description
(No Model.) 2 Sheet-sSheet 1.
J. B. WILKINSON.
APPARATUS FOR DEFEOATING SAGCHARINE JUICE.
N0. 588,521. Patented Aug. 17, 1897:
2 Sheets-Sheet 2.
' J. WILKINSON. APPARATUS FOR DEFEGATING SAGOHARINE JUICE.
(No Model.)
. N0. 588,521. Patented Aug. 17,1897.
UNITED STATES JOSEPH BIDDLE WVILKIN SON, OF NEW ORLEANS, LOUISIANA.
APPARATUS FOR DEFECATING SACCHARIN E JU ICES.
SPECIFICATION forming part of Letters Patent No. 588,521, dated 'August 17, 1897.
7 Application filed February 28, 1896. Serial No. 581,178. (No model.)
To all whom it may concern:
Be it known that [,JOSEPH BIDDLE WILKIN- SON, a citizen of the United States, residing at New Orleans,in the parish of Orleans and State of Louisiana, have invented certain new and useful Improvements in Olarifiers and Defecators; and I do hereby declare the following to be a full, clear, and exact description of the invention, such as will enable others skilled in the art to which it appertains to make and use the same.
My invention relates to improvements in apparatus for the defecation of cane-juice; and it consists of certain novel features hereinafter described and claimed.
The quality of sugar is largely determined by the clarification of the cane-juice.
To make good sugar, it is essential to have good clarification as a preliminary step. Other things being equal the better the clarification the better will be the sugar made. Not only this, but the quantity of sugar obtained from a given quantity of cane-juice will be proportionately increased with the degree of improved clarification unless clarifiants be used destructive to the-crystalline character of the cane sugar.
There are two prominent processes employed in the clarification of cane-juice, both supplemented by chemical reagents. One is to cause its impurities through heat to rise and fioat on its surface, the other to cause a portion of the impurities to separate and through gravitation to settle on the bottom or near the bottom of the clarifying vessel. This last is known as precipitation or sedimentation, and my invention relatesespecially to this latter process. The usual practice is to bring up the can e-j nice to the boiling-point or a trifle below the same and to remove the scum which arises with a skimmer, continuing this process with the cane-juice at or near the point of ebullition until, in the judgmentof the operator, the juice is sufficiently defecated. The heat is then shut off and the juice is then allowed to remain for a time to settle or is drawn off into what are called precipitators or settling-tanks. The objections urged against this continued skimming process are that boiling excites constant currents of .circulation in the juice, breaking up the particles of coagulated matter which juice ensues that of precipitation.
had been brought into a state of mechanical suspension by the heat applied, and thatv these currents through the juice keep these particles of impurities in such constant agitation as to prevent-their proper separation from the body of the juice. It is well known that the more minute the particles of matter, are in a state ofmechanical suspension in. a fluid the more difficult is it to effect their separation from the fluid. Thus particles can beso finely divided that they will remain permanently suspended in a fluid or even in air, although the medium in which they are suspended be in a state of perfect rest. As these particles in cane-juice are, according to their amount, more or less obstructive to the formation ofsugar of a high standard and have also a chemical character damaging not only to the qualitybut to the quantity of sugar, it becomes important as far as possible to remove them.
Following the process of skimming the As commonly practiced this is entirely inadequate to the end desired and fraught with various objections. Generally the skimmed juice is allowed to settle for a short time in the clarifier after being skimmed and then drawn off into other tanks for further precipitation or immediately into the concentratingpans. This process is open to the following objections: First, the time allowed for effective precipitation is not sufficient for this purpose; second, deeantation at the time of precipitation by breaking up the particles of coagulated matter renders their further separation more difficult and perhaps impossible, and,
further, the sedimentation in open vessels presents the serious objection that exposure of the juice to the air subjects it to the danger of molecular changes through fermentation, this increasing in degree as the exposure is prolonged. It is safe to afiirm that no juice can be allowed to remain a sufficient length of time in open vessels for proper precipitation without serious loss (through molecular changes) in quantity and quality of sugar. Cane-juice as run from the clarifiers and left in the open settling-tanks is in a most favorable condition for-fermentation.
Fermentation is slow to take place below Fahrenheit and is arrested at a temperature somewhat below the boiling-point. It is most favored between and 100. These data, then, taken from standard authorities, show that the valuable adjunct of clarification through precipitation in open tanks is surrounded with dangers and open to various objections. If the juice is hurried forward, precipitation is interfered with or arrested. If left long enough in the open tanks the evils, of fermentation ensue.
In the manufacture of sugar fermentation is believed to be the manufacturefis greatest foe. Could this evil be arrested he would have little difficulty in bringing his work in sugar-making to a high degree of perfection. The agents of fermentation are at work upon the juice as it runs from the mill and threaten it at almost every stage of its journey in its transformation into crystalline matter. It is a mistake to suppose that ferinents have only done their evil work when these effects become apparent to our sight and taste. These are but the emphasized expressions of the ferments assaults upon the sweet liquid, the insidious foe had been at work long before. From these premises it follows that the canejuice should be hurried as rapidly as possible from the mill to the clarifier, and that the process of clarification should be done in closed vessels to exclude the air and in vessels of sufficient strength to bear safely at pressure of about fifteen pounds to the square inch above atmospheric pressure. Two advantages are presented by this procedure. First, the exclusion of the air would allow much longer time for precipitation of the impurities of the heated juice; second, heated to a higher temperature under pressure the protein or albuminose matter, so important to engender fermentation, would be more thoroughly separated and the germs of organic life necessary to produce fermentation more certainlydestroyed. (Jane-juice thus acted upon in closed vessels could be kept, as regards time, almost indefinitely without fermentation. The preservation of meats, fruits, and vegetables in sealed cans for long periods of time illustrate the value of clarifying cane-juice under conditions preventive of fermentation. In this method greater time would also be allowed to separate the impurities from its saccharine matter than that practiced in open vessels through skimming and precipitation.
The mechanism best adapted to the clarification of juice in closed vessels may present itself in different forms to different persons, but I have shown one form of a pparatus which I believe suitable for this purgose.
Reference is bad to the accompanying drawings, in which the same parts are indicated by the same letters throughout the several views.
Figure l'represents the apparatus in elevation. Many of the non-essential elements are omitted and the apparatus is shown diagrammatically. Fig. 2 represents a central in any convenient way, and in which the lime or other chemical reagents are added to the juice before it is carried over to the elarifiers. There should be enough of these tanks A to allow them to be frequently washed out, so that fermentation may be as far as possible avoided before the juice gets to the clarifiers. The juice is pumped from these tanks A through the branch pipes b and the main pipe B to the pump 0, whence it is delivered through the pipe D and the branches d to the clarifiers E. These various main and branch pipes are provided with valves wherever required, and so, in fact, are all the pipes in the system, and it will not be necessary to refer to these valves specifically.
The clarifiers E are preferably made of a cylindrical shell E with spherical bottom E and dome-shaped top E and both top and bottom are secured to the cylindrical shell, so as to make a steam-tight joint, as by bolts 6, or in any other convenient way. The top E is made detachable for purposes of occasional cleaning out, and is preferably provided with an eyebolt e, to which a tackle can be hooked, whereby the top may be conveniently lifted off after the bolts 0 are unscrewed. This top or cap E is also preferably provided with a valve-seat c for the safety-valve Q, but this valve-may be connected to the shell E or attached to the clarifier in any convenient way.
The heated juice is drawn from the clarifierthrough the branch pipesfand the pipes F into the pipe G, whence it is delivered through the pipes g to the tanks II, from which tanks the clarified juice is pumped to the vacuum pans or other concentrating apparatus. (Not shown.) The settlings in the bottoms E are drawn off through the pipes 70 into the pipe K, whence they are delivered through the pipes it into the tanks L. The clearer portion of the liquid in the tanks L is drawn off through the pipe M, while the more turgid portions are drained through the pipes 77 and the main pipe N to the filter-press P, which is operated in the usual well-known way.
The juice in the elarifiers is heated by a steam-pipe, preferably in the form of a coil R, the steam being fed in through the pipes r and controlled by the valve r, while the condensed water from this coil R either escapes, as at r", or is led to the hot-well by any suitable pipe. (Not shown.) Any other arrangement of heating-pipes may be adopted, if preferred.
Sight-tubes S are preferably provided on each clarifier, but these are not absolutely necessary. In practice it would be preferable to have a sufficient number of the clarifiers to allow the heated juice to cool slowly and to settle gradually, but if it be desired to expedite the process of cooling a waterjacket T, inclosing each clarifier or a part thereof, may be added to the apparatus, if desired. Thus I have shown such a waterjacket, which is illustrated in detail in Fig. 2, the cold water being fed in through the pipe and. escaping through the pipe i, but this water-jacket would not ordinarily be necessary.
For purposes of cleaning out the clarifier and to avoid removing the cover E more often than is absolutely necessary I provide a wash-out pipe W for water and a steam-pipe V for injecting steam into the clarifier after the juice has been withdrawn therefrom. In order to obtain the best effects from this jet of steam or water, the same may be either provided with roses or they may be provided with orifices set at an angle to the inner surface of the cylindrical shell, whereby a spiral or vertical direction may be given to the steam or Water, and thus the various parts of the interior of the shell may be more thoroughly cleansed than were these jets to be projected directly in toward the center of the clarifier. These steam and water pipes should also preferably be so arranged that a hose may be coupled onto the same when the top E is removed, and thus each and every part of the interior of the clarifier may be reached by the steam or water, or both.
In the operation of the device the clarifier is filled with juice very nearly to the top of the cylindrical portion, and then steam is turned on to the heating-coil R. The heat is continued until a pressure of about fifteen pounds above that of the atmosphere is attained on the inside of the clarifier, at which pressure the temperature of the liquidsis about 240 Fahrenheit, prior to which time all of the albumen will have been coagulated. This pressure may be noted either from an ordinary pressure-gage (not shown) attached to the clarifier, or from the blowing off of the safety-valve Q. After the heatedjuice has remained long enough to cool and V settle sufficiently the clearer portions are drawn off through the pipes f, while the scum and sediment are drawn off through the pipe 715, as has been hereinbefore described.
After discharging, each clarifier'should be either washed out through the steam and water pipes already mentioned, or the tops may be periodically removed and the clariffer thoroughly cleaned out.
By having a large vessel, which is heated and cooled gradually, the connection-currents are not violent and the solid particles are not broken up so fine as to fail to be readily precipitated during the process of cooling.
The exclusion of the air prevents the molecular changes due to fermentation. The application of the high heat is destructive to those forms of germ-life upon which fermentation depends. These are some of the principal advantages of my improved process and apparatus, to which may be added the maintenance of the exclusion of air and the preservation of the juice at a temperature above that which permits fermentation for a sufficient length of time to permit more perfect free precipitation of the coagulated elements of the juice, the employment of a higher degree of heat to coagulate the vegetable albuminoids than is possible in open vessels, where the separation of these impurities is only partiahand the quiescent condition of the juice during the process of precipitation, as well as the simplicity of the operation of clarification in closed vessels.
Having thus described my invention,what I claim, and desire to secure by Letters Patent of'the United States, is
1. In an apparatus for defecatin g and clarifying cane-juice, a closed vessel adapted to withstand internal pressure,a pump and pipes for supplying juice to said vessel, a steamcoil mounted in said vessel near the base thereof and adapted to heat said juice from contact with the exterior of said steam-coil,
pipes for drawing ofi the clearer portion of the juice after it has been settled, and a separate pipe for drawing off the sediment from the base of said vessel, and a jacket inclosing the sides of said vessel, with means for injecting fluid into said jacket for cooling the contents of said vessel, substantially as described.
2. In an apparatus for defecating and clarifying cane-juice, a closed vessel adapted to withstand internal pressure,a pump and pipes for supplying juice to said vessel, a steamcoil mounted in said vessel near the base thereof and adapted to heat said juice from contact with the exterior of said steam-coil, pipes opening into the said vessel near the base thereof for drawing off the clearer portion of the juice after it has settled, and a separate pipe opening into the base of said vessel for drawing off the sediment, anda jacket inclosing the sides of said vessel,with means for injecting fluid into said jacket for cooling the contents of said vessel, substantially as described.
3. In an apparatus for defecating and clarifying cane-j uice, a closed vessel provided with a steam-tight top entirely removable, and a safety-valve, a pump and pipes for supplying juice to said vessel and for drawing off the juice therefrom when desired, and a steamcoil mounted in the said vessel near the base thereof and an opening through the sides of said vessel, and adapted to heat the juice by contact with the exterior of said coil, and a jacket inclosing the sides of said vessel,with means for injecting fluid into said jacket for cooling the contents of said vessel, substantially as described.
4. In an apparatus for defecating and clarifying cane-juice, a closed vessel with a steamtight top wholly removable, and a curved bottom, a pump and pipes for supplying juice to said vessel, a steam-coil mounted in said vessel near the base thereof and adapted to heat IIO the juice from contact with the exterior of said coil, pipes mounted in the sides of said Vessel near the base thereof for drawing off the clearer portion of the juice after it has settled, and a separate pipe connected to the lower portion of the curved bottom and adapted to draw off the sediment from the said Vessel, and a jacket inclosing the sides of said vessehwith means for in jecting fluid into the said jacket for cooling the contents of said 10 vessel, substantially as described.
In testimony whereof I afiix my signature in presence of two witnesses.
JOSEPH BIDDLE WILKINSON.
Witnesses:
E. H. BINDLEY, Jr,
l l i i l JOHN J. SANCIE.
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US588521A true US588521A (en) | 1897-08-17 |
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Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2008091878A1 (en) | 2007-01-22 | 2008-07-31 | Altea Therapeutics Corporation | Transdermal porator and patch system and method for using same |
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- US US588521D patent/US588521A/en not_active Expired - Lifetime
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2008091878A1 (en) | 2007-01-22 | 2008-07-31 | Altea Therapeutics Corporation | Transdermal porator and patch system and method for using same |
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