US601305A - Henri armand joseph manourt - Google Patents
Henri armand joseph manourt Download PDFInfo
- Publication number
- US601305A US601305A US601305DA US601305A US 601305 A US601305 A US 601305A US 601305D A US601305D A US 601305DA US 601305 A US601305 A US 601305A
- Authority
- US
- United States
- Prior art keywords
- sugar
- juice
- joseph
- henri
- armand
- 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
- 239000007788 liquid Substances 0.000 description 26
- QVQLCTNNEUAWMS-UHFFFAOYSA-N Barium oxide Chemical compound [Ba]=O QVQLCTNNEUAWMS-UHFFFAOYSA-N 0.000 description 20
- 229910001864 baryta Inorganic materials 0.000 description 20
- 239000002585 base Substances 0.000 description 16
- BVKZGUZCCUSVTD-UHFFFAOYSA-N Carbonic acid Chemical compound OC(O)=O BVKZGUZCCUSVTD-UHFFFAOYSA-N 0.000 description 10
- 235000008733 Citrus aurantifolia Nutrition 0.000 description 10
- 235000015450 Tilia cordata Nutrition 0.000 description 10
- 235000011941 Tilia x europaea Nutrition 0.000 description 10
- 239000004571 lime Substances 0.000 description 10
- 241000209134 Arundinaria Species 0.000 description 8
- 238000009835 boiling Methods 0.000 description 8
- 235000013379 molasses Nutrition 0.000 description 8
- IATRAKWUXMZMIY-UHFFFAOYSA-N Strontium oxide Chemical compound [O-2].[Sr+2] IATRAKWUXMZMIY-UHFFFAOYSA-N 0.000 description 6
- 150000001875 compounds Chemical class 0.000 description 6
- 238000002425 crystallisation Methods 0.000 description 6
- 230000005712 crystallization Effects 0.000 description 6
- 238000004519 manufacturing process Methods 0.000 description 6
- 238000000034 method Methods 0.000 description 6
- 229940072033 potash Drugs 0.000 description 6
- BWHMMNNQKKPAPP-UHFFFAOYSA-L potassium carbonate Substances [K+].[K+].[O-]C([O-])=O BWHMMNNQKKPAPP-UHFFFAOYSA-L 0.000 description 6
- 235000015320 potassium carbonate Nutrition 0.000 description 6
- KWYUFKZDYYNOTN-UHFFFAOYSA-M potassium hydroxide Chemical compound [OH-].[K+] KWYUFKZDYYNOTN-UHFFFAOYSA-M 0.000 description 6
- 239000003513 alkali Substances 0.000 description 4
- 238000001914 filtration Methods 0.000 description 4
- 229910052500 inorganic mineral Inorganic materials 0.000 description 4
- 239000011707 mineral Substances 0.000 description 4
- 235000010755 mineral Nutrition 0.000 description 4
- 239000000203 mixture Substances 0.000 description 4
- 239000012452 mother liquor Substances 0.000 description 4
- 239000002244 precipitate Substances 0.000 description 4
- 239000000126 substance Substances 0.000 description 4
- 239000006188 syrup Substances 0.000 description 4
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 4
- 235000016068 Berberis vulgaris Nutrition 0.000 description 2
- 241000335053 Beta vulgaris Species 0.000 description 2
- CVHZOJJKTDOEJC-UHFFFAOYSA-N Saccharin Chemical compound C1=CC=C2C(=O)NS(=O)(=O)C2=C1 CVHZOJJKTDOEJC-UHFFFAOYSA-N 0.000 description 2
- 230000015271 coagulation Effects 0.000 description 2
- 238000005345 coagulation Methods 0.000 description 2
- 230000001419 dependent Effects 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 238000003379 elimination reaction Methods 0.000 description 2
- 238000001704 evaporation Methods 0.000 description 2
- 239000012530 fluid Substances 0.000 description 2
- 235000011837 pasties Nutrition 0.000 description 2
- 238000000746 purification Methods 0.000 description 2
- 238000007670 refining Methods 0.000 description 2
- 238000009877 rendering Methods 0.000 description 2
- 235000020357 syrup Nutrition 0.000 description 2
Classifications
-
- C—CHEMISTRY; METALLURGY
- C13—SUGAR INDUSTRY
- C13B—PRODUCTION OF SUCROSE; APPARATUS SPECIALLY ADAPTED THEREFOR
- C13B20/00—Purification of sugar juices
- C13B20/005—Purification of sugar juices using chemicals not provided for in groups C13B20/02 - C13B20/14
Definitions
- This invention relates to an improved method of utilizing molasses in the manufacture of sugar; and it has for its object to'furnish simple and practical means for crystallizing and obtaining as first sugarthat is to say, by means of a single boiling almost the whole sugar contained in the beet root or sugar-canewhile reducing to a large extent the quantity offinal molasses ordinarily produced.
- I may also indicate that I am not unaware that alkaline earthy base ssuch as baryta, strontia, or 1ime.have been alreadyemployed for converting into sucrate the sugar contained in the liquids or syrups arising from the centrifuging of the masse-cuite and that this insoluble sucrate after having been separated by suitable filtration and washed was then decomposed by carbonic acid or even 1 utilized for purifying the juice of beet-root or cane; but in my improved process I do not propose to form sucrate of lime, baryta, or strontia. On the contrary, I employ these alkaline earthy bases only in a suitable proportion for obtaining a kind of purification as a result of the following observations.
- alkaline earthy base s such as baryta, strontia, or 1ime.have been alreadyemployed for converting into sucrate the sugar contained in the liquids or syrups arising from the centrifuging of the masse-cuite and that this insoluble sucrate after having been separated by suitable
- barytie liquid is preferably effected at two periodsat the commencement of the two ordinary periods of the carbonation-and is carried out in the following manner:
- the carbonic acid By the first action of the carbonic acid the excess of alkaline earthy base free or in combination with the sugar is precipitated.
- the corbonation is arrested in such a way that the liquid is still strongly alkaline, which maintains the insolubility of the barytic organic or mineral insoluble compounds hereinbefore mentioned.
- the clear juice is separated by filtration in filter-presses from the precipitate formed.
- This clear juice is then subjected to a second carbonation with the addi-' tion of a fresh quantity of barytic liquid, and after this fresh ebullition the mass is again passed through filter-presses in order to separate the precipitate from the clear juice, which then undergoes the ordinary operations of evaporation and boiling.
- the centrifuging includes no clarifying with water or steam, and only liquors poor in sugar are obtained.
- these poor liquors are treated, as before, with a solution of baryta in such a way as to introduce about five kilograms of crystallized baryta per one hundred liters of the said poor liquors, and only about two liters of these alkaline liquids per one hundred liters of juice are introduced before or after they have received the lime necessary for the carbonation.
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Life Sciences & Earth Sciences (AREA)
- Biochemistry (AREA)
- Organic Chemistry (AREA)
- Confectionery (AREA)
Description
UNITED STATES PATENT OFFICE HENRI ARMANn JOSEPH'MANOURY, OF PARIS, FRANCE.
PROCESS OF DEFECATING SUGAR-JUICES.
SPECIFICATION forming part of Letters Patent No. 601,305, dated March 29, 1898.
Application filed June 23, 1897. Serial No. 641,948. (No specimens.) Patented in France September 29, 1896, No. 260,081; in Belgium November 9, 1896, No. 124,496; in Germany November 11, 1896,No. 18,892; in Spain November 17, 1896,110- 19,954; in Russia. November 27, 1896, No. 694; in Austria November 30, 1896, No. 46/5,191, and in Hungary April15,
1 outs in France, No. 260,081, dated September 29, 1896, patent of addition, dated October 31 1896; in Belgium, No.124,496, dated November 9, 1896; in Spain, No. 19,954,dated November 17 1896; in Germany, dated November 11,
1896, Serial No. M. 13,392 /89'6; in Austria, No. 46/5,I91, dated November 30, 1896; in Hungary, No. 8,009, dated April 15, 1897, and in Russia, Serial No. 694, dated'November l5 and 27, 1896,) of which the following is a specification.
This invention relates to an improved method of utilizing molasses in the manufacture of sugar; and it has for its object to'furnish simple and practical means for crystallizing and obtaining as first sugarthat is to say, by means of a single boiling almost the whole sugar contained in the beet root or sugar-canewhile reducing to a large extent the quantity offinal molasses ordinarily produced.
It consists, essentially, in introducing into the beet-root juice or cane-juice a suitable proportion of liquids more or less rich in sugar from the centrifuging of the masse-cuite after they have been subjected to the action of an alkaline earthy base, such as baryta, strontia,
or lime.
. the more or less rich drain-syrups aforesaid,
which I treat with the alkaline earthy bases and then add to the juice of beet-root or cane, and .the poorer liquids obtained at the commencement of the centrifuging may be introduced with advantage into the boiling-down pan toward the end of the boiling in a proportion dependent on the degree of poverty of sugar which it is desired to obtain in the mother-liquor of crystallization of the sugar.
I may also indicate that I am not unaware that alkaline earthy base ssuch as baryta, strontia, or 1ime.have been alreadyemployed for converting into sucrate the sugar contained in the liquids or syrups arising from the centrifuging of the masse-cuite and that this insoluble sucrate after having been separated by suitable filtration and washed was then decomposed by carbonic acid or even 1 utilized for purifying the juice of beet-root or cane; but in my improved process I do not propose to form sucrate of lime, baryta, or strontia. On the contrary, I employ these alkaline earthy bases only in a suitable proportion for obtaining a kind of purification as a result of the following observations.
I have ascertained that the alkaline earthy basessuch as baryta, lime, or strontia-introduced into the liquids arising from the centrifuging are substituted for the potash and soda existing in the organic or mineralcompounds which are contained in these liquids, forming insoluble compounds, and that on the other hand the potash and soda thus set at liberty may be in turn eliminated by means of albuminoid substances contained in the beet-root oroane juice, the coagulation of which resulting from the action of the said alkalies (potash and soda) and of heat removes these alkalies in the form of insoluble or soluble compounds in the coagulum obtained.
I will now describe the method of carrying ject to be obtained, and I operate in the following manner: In a tank provided with a steam-agitator I prepare a solution containing fifteen kilograms of baryta per one hundred kilograms of water. The proportion of this solution which must be added to the rich liquids hereinbefore mentioned is variable according as they are more or less impure. Generally speaking, this quantity must be such that these liquids receive a quantity of baryta equal to about five per cent. of their weight. The baryta liquid prepared in the manner mentioned is run into the crude juice of beet-root or cane before or after it has received the quantity of lime usually necessary for the carbonation. This addition of barytie liquid is preferably effected at two periodsat the commencement of the two ordinary periods of the carbonation-and is carried out in the following manner: By the first action of the carbonic acid the excess of alkaline earthy base free or in combination with the sugar is precipitated. Then the corbonation is arrested in such a way that the liquid is still strongly alkaline, which maintains the insolubility of the barytic organic or mineral insoluble compounds hereinbefore mentioned. Then the clear juice is separated by filtration in filter-presses from the precipitate formed. This clear juice is then subjected to a second carbonation with the addi-' tion of a fresh quantity of barytic liquid, and after this fresh ebullition the mass is again passed through filter-presses in order to separate the precipitate from the clear juice, which then undergoes the ordinary operations of evaporation and boiling.
As already stated, I prefer to complete the operation by introducing into the boilingdown pan, toward the end of the boiling, a quantity of poor liquids arising from the centrifuging of the previously-formed massecuite with a view to rendering more fluid the pasty mass contained at this moment in the boiling-down pan, thus facilitating the crystallization of the sugar contained in the mother-liquor.
\Vhen only stained sugar intended for refining purposes is made, the centrifuging includes no clarifying with water or steam, and only liquors poor in sugar are obtained. In this case these poor liquors are treated, as before, with a solution of baryta in such a way as to introduce about five kilograms of crystallized baryta per one hundred liters of the said poor liquors, and only about two liters of these alkaline liquids per one hundred liters of juice are introduced before or after they have received the lime necessary for the carbonation.
In the description just given I have indicated that the drainings of the centrifuging were rendered alkaline by means of alkaline earthy bases before being introduced into the crude beet-root juice; but it must be thoroughly understood that these drainings may be mixed directly with the said juice and alkaline earthy bases be caused to act in suitable proportions on the mixture obtained, and that it is also possible to introduce first the alkaline earthy bases into the saccharine juice and to then add a suitable quantity of the drainings from the centrifuging. The result obtained remains evidently the same in both cases. It is therefore evident that as the process has for its effect the elimination at little expense of a considerable proportion of the foreign organic and mineral matters or substances contained in the drainings from the centrifuging there results 011 the one hand a crystallization in the form of first sugar of a greater part of the sugar contained in the beet-root or cane and on the other hand a reduction in the quantity of final molasses to a degree which has never yet been attained with the improved methods of sugar manufacture at present in use.
I declare that what I claim is- The herein-described method of utilizing molasses in the manufacture of sugar, consisting in introducing into the crude juice before carbonation a suitable proportion of drainings from the eentrifugin g of the massecuite with the addition of baryta in suitable proportions.
In testimony whereof I have signed my name to this specification in the presence of two subscribing witnesses.
HENRI ARMAND JOSEPH MANOURY.
IVitnesses:
LoUls TAILFER, JACQUES CoNDsINY.
Publications (1)
Publication Number | Publication Date |
---|---|
US601305A true US601305A (en) | 1898-03-29 |
Family
ID=2669942
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
US601305D Expired - Lifetime US601305A (en) | Henri armand joseph manourt |
Country Status (1)
Country | Link |
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US (1) | US601305A (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3542591A (en) * | 1969-05-14 | 1970-11-24 | Braunschweigische Masch Bau | Purification of sugar juice |
US4492601A (en) * | 1982-10-15 | 1985-01-08 | Daiichi Seito Kabushiki Kaisha | Process for clarifying and desalinating sugar cane syrup or molasses |
-
0
- US US601305D patent/US601305A/en not_active Expired - Lifetime
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3542591A (en) * | 1969-05-14 | 1970-11-24 | Braunschweigische Masch Bau | Purification of sugar juice |
US4492601A (en) * | 1982-10-15 | 1985-01-08 | Daiichi Seito Kabushiki Kaisha | Process for clarifying and desalinating sugar cane syrup or molasses |
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