КРИСТАЛЛИЗАТОР

Кристаллизатор, состоящий из двустенной ванны, снабженной мешалкой и крышкой, отличающийся тем, что добавочно содержит устройство для магнитной обработки сиропа. РОССИЙСКАЯ ФЕДЕРАЦИЯ (19) RU (11) 107 157 (13) U1 (51) МПК C13B 30/02 (2011.01) ФЕДЕРАЛЬНАЯ СЛУЖБА ПО ИНТЕЛЛЕКТУАЛЬНОЙ СОБСТВЕННОСТИ, ПАТЕНТАМ И ТОВАРНЫМ ЗНАКАМ (12) ОПИСАНИЕ ПОЛЕЗНОЙ МОДЕЛИ К ПАТЕНТУ (21)(22) Заявка: 2010130944/15, 23.07.2010 (24) Дата начала отсчета срока действия патента: 23.07.2010 (45) Опубликовано: 10.08.2011 R U 1 0 7 1 5 7 Формула полезной модели Кристаллизатор, состоящий из двустенной ванны, снабженной мешалкой и крышкой, отличающийся тем, что добавочно содержит устройство для магнитной обработки сиропа. Ñòðàíèöà: 1 ru CL U 1 U 1 (54) КРИСТАЛЛИЗАТОР 1 0 7 1 5 7 Адрес для переписки: 160555, г.Вологда, с. Молочное, ул. Шмидта, 2, ФГОУ ВПО ВГМХА им. Н.В. Верещагина, отдел науки (73) Патентообладатель(и): Федеральное государственное образовательное учреждение высшего профессионального образования "Вологодская государственная молочнохозяйственная академия им. Н.В. Верещагина" (RU) R U Приоритет(ы): (22) Дата подачи заявки: 23.07.2010 (72) Автор(ы): Топал Ольга Ивановна (RU) RU 5 10 15 20 25 30 35 40 45 50 107 157 U1 Предлагаемое устройство относится к оборудованию молочной промышленности, в частности к аппаратам для кристаллизации молочного сахара. Известны следующие аппараты, используемые для кристаллизации: - циркуляционный охладительный кристаллизатор [1], - устройство для кристаллизации [2], - кристаллизатор [3], - каскадный кристаллизатор непрерывного действия [4], - кристаллизатор [5], - аппарат для кристаллизации лактозы из раствора [6], - кристаллизатор для лактозы [7], - кристаллизатор для лактозы [8], - установка для кристаллизации лактозы [9]. Недостатками перечисленных кристаллизаторов являются: большие габаритные размеры и масса аппаратов, неудобство в обслуживании, значительные энергозатраты, высокая стоимость. В настоящее время на предприятиях молочной промышленности при ...

МЕШАЛКА-КРИСТАЛЛИЗАТОР С ВОЗДУШНЫМ ОХЛАЖДЕНИЕМ

Мешалка-кристаллизатор с воздушным охлаждением, состоящая из горизонтального корытообразного корпуса, в котором вращается вал с укрепленными на нем перемешивающими лопастями, на которых закреплены лопатки, установленные наклонно относительно лопастей для придания утфелю импульса движения в сторону выгрузного отверстия мешалки, отличающаяся тем, что над мешалкой-кристаллизатором установлена система воздуховодов для охлаждения утфеля путем подачи охлажденного воздуха непосредственно на его поверхность. РОССИЙСКАЯ ФЕДЕРАЦИЯ (19) RU (11) (51) МПК C13B 30/00 (13) 114 053 U1 (2011.01) ФЕДЕРАЛЬНАЯ СЛУЖБА ПО ИНТЕЛЛЕКТУАЛЬНОЙ СОБСТВЕННОСТИ (12) ОПИСАНИЕ (21)(22) Заявка: ПОЛЕЗНОЙ МОДЕЛИ К ПАТЕНТУ 2011129096/13, 13.07.2011 (24) Дата начала отсчета срока действия патента: 13.07.2011 (72) Автор(ы): Спичак Василий Варфоломеевич (RU), Вратский Анатолий Михайлович (RU) (45) Опубликовано: 10.03.2012 Бюл. № 7 R U 1 1 4 0 5 3 Формула полезной модели Мешалка-кристаллизатор с воздушным охлаждением, состоящая из горизонтального корытообразного корпуса, в котором вращается вал с укрепленными на нем перемешивающими лопастями, на которых закреплены лопатки, установленные наклонно относительно лопастей для придания утфелю импульса движения в сторону выгрузного отверстия мешалки, отличающаяся тем, что над мешалкойкристаллизатором установлена система воздуховодов для охлаждения утфеля путем подачи охлажденного воздуха непосредственно на его поверхность. Стр.: 1 U 1 U 1 (54) МЕШАЛКА-КРИСТАЛЛИЗАТОР С ВОЗДУШНЫМ ОХЛАЖДЕНИЕМ 1 1 4 0 5 3 Адрес для переписки: 305029, г.Курск, ул. К. Маркса, 63, ГНУ РНИИСП Россельхозакадемии R U (73) Патентообладатель(и): Государственное научное учреждение Российский научно-исследовательский институт сахарной промышленности Россельхозакадемии (ГНУ РНИИСП Россельхозакадемии) (RU) Приоритет(ы): (22) Дата подачи заявки: 13.07.2011 RU 5 10 15 20 25 30 35 40 45 114 053 U1 Полезная модель относится к сахарному производству, в частности, к оборудованию для кристаллизации ...

МЕШАЛКА-КРИСТАЛЛИЗАТОР ПЕРИОДИЧЕСКОГО ДЕЙСТВИЯ

Мешалка-кристаллизатор периодического действия, установленная на вертикальном валу, расположенном в циркуляционном канале тепловой камеры вакуум-аппарата, и состоящая из диска, имеющего радиально расположенные окна, снабженные наклонными лопатками, жестко закрепленные с диском и расположенные вогнутой поверхностью к окнам, отличающаяся тем, что диск закреплен на вертикальном валу, установленном в циркуляционном канале сверху, обеспечивающем центрирование мешалки в тепловой камере. И 1 122651 ко РОССИЙСКАЯ ФЕДЕРАЦИЯ 7 ВУ” 122 651” 1 ФЕДЕРАЛЬНАЯ СЛУЖБА ПО ИНТЕЛЛЕКТУАЛЬНОЙ СОБСТВЕННОСТИ (12) ИЗВЕЩЕНИЯ К ПАТЕНТУ НА ПОЛЕЗНУЮ МОДЕЛЬ ММ9К Досрочное прекращение действия патента из-за неуплаты в установленный срок пошлины за поддержание патента в силе Дата прекращения действия патента: 14.03.2019 Дата внесения записи в Государственный реестр: 28.01.2020 Дата публикации и номер бюллетеня: 28.01.2020 Бюл. №4 Стр.: 1 па рч9ссу ЕП

Устройство для предподготовки раствора к кристаллизации

Настоящее техническое решение относится к оборудованию для кристаллизации различных веществ в биотехнологической и химической промышленностях и может быть применено для выделения кристаллизацией продуктов микробиологического синтеза, продуктов сахарной промышленности, солей и других веществ, кристаллизуемых из растворов. Заявленное устройство для предподготовки раствора к кристаллизации содержит ультразвуковой аэродинамический распылитель - генератор аэрозоля, представляющий собой газоструйный излучатель, в активную зону которого подается жидкость - концентрируемый раствор; рабочую емкость с кулисами внутри нее, направляющими потоки аэрозоля и паровоздушной смеси; выводной патрубок для сконцентрированной и охлажденной жидкости, представляющей собой сконденсированный аэрозоль; выводной патрубок для паровоздушной смеси. Характерная особенность устройства - распыление подготавливаемой к кристаллизации жидкости ультразвуковым аэродинамическим генератором аэрозолей с последующей конденсацией аэрозоля в подготовленный к процессу кристаллизации раствор. РОССИЙСКАЯ ФЕДЕРАЦИЯ (19) RU (11) (13) 176 550 U1 (51) МПК C30B 35/00 (2006.01) C30B 7/00 (2006.01) B01D 9/02 (2006.01) B01J 19/10 (2006.01) C13B 30/02 (2011.01) ФЕДЕРАЛЬНАЯ СЛУЖБА ПО ИНТЕЛЛЕКТУАЛЬНОЙ СОБСТВЕННОСТИ (12) ОПИСАНИЕ ПОЛЕЗНОЙ МОДЕЛИ К ПАТЕНТУ (52) СПК C30B 35/007 (2017.08); C30B 7/00 (2017.08); B01D 9/02 (2017.08); B01D 2259/10 (2017.08); B01D 2259/816 (2017.08); B01J 19/10 (2017.08); B01J 2219/00011 (2017.08); C13B 30/02 (2017.08) (21)(22) Заявка: 2017128915, 15.08.2017 15.08.2017 Дата регистрации: 23.01.2018 (45) Опубликовано: 23.01.2018 Бюл. № 3 1 7 6 5 5 0 R U (56) Список документов, цитированных в отчете о поиске: US 7531131 В2, 12.05.2009. SU 1084038 А1, 07.04.1984. EP 2055197 В1, 20.05.2015. CHINMAY N. GAJENDRAGADKAR et al, Intensified recovery of valuable products from whey by use of ultrasound in processing steps - A review, "Ultrasonics Sonochemistry", 2016, Vol. 32, p.p. 102-118. (54) Устройство для ...

UNIVERSAL BIOMASS REFINERY

The invention is directed to a process for refining prepared biomass to produce hemicellulose hydrolyzates, cellulose or sugars involving the perforate at least a portion of the cells of the prepared biomass prior to hydrolyzing the biomass, reclaiming the catalysts used in hydrolysis for further hydrolysis, and drying the hydrolysis using reclaimed heat from previous steps in the process. 149-. (canceled)50. A process for refining biomass , the process comprising the steps of: (i) forming a first slurry from the biomass having a first solids portion comprising hemicellulose and cellulose, and having a first liquid portion;', '(ii) adding an alkaline catalyst and applying heat and either mechanical shear or cavitation to the first slurry;', '(iii) mechanically separating the first solids portion from the first liquid portion; and', '(iv) combining the first liquid portion with additional biomass and repeating steps (a)(ii) and (a)(iii) until a threshold concentration of extractable products in the first liquid extraction is achieved;, 'a. performing a first hemicellulose hydrolysis by (i) combining the first solids portion and a catalyst in a second slurry having a second solids portion comprising cellulose, and a second liquids portion comprising hemicellulose hydrolyzates in solution, and applying mechanical shear or cavitation to the second slurry;', '(ii) mechanically separating the second solids portion from the second liquid portion;', '(iii) recovering the catalyst from the second liquid portion;', '(iv) repeating steps (b)(i) and (b)(ii), using, in step (b)(i) the second solids portion recovered in step (b)(ii) as the first solids portion and the catalyst recovered in step (b)(iii), adding additional catalyst or fresh biomass to maintain a minimum specified concentration of catalyst., 'b. performing a second hemicellulose hydrolysis by51. The process of claims 50 , wherein the first solids portion or the second solids portion comprise lignin claims 50 , ...

METHOD OF PRODUCING SUGARS USING A COMBINATION OF ACIDS TO SELECTIVELY HYDROLYZE HEMICELLULOSIC AND CELLULOSIC MATERIALS

A method is provided for producing sugars using a combination of acids to hydrolyze hemicellulosic and cellulosic materials in biomass, said combination of acids namely comprising a first, weak organic acid (such as acetic acid or formic acid) for providing a pentose product or stream from hydrolyzing hemicellulosic materials in the biomass on a batchwise, semi-continuous or continuous basis, and a second, strong mineral acid (such as sulfuric acid) for providing a hexose product or stream from hydrolyzing cellulosic materials in the biomass. 1. A method of processing a lignocellulosic biomass including cellulose , hemicellulose and lignin fractions , comprising the steps of:applying a weak organic acid to the biomass to at least partly depolymerize the hemicellulosic and lignin materials in the biomass;drying the weak-acid treated biomass to provide a sufficiently high solids content material as to be pelletized;pelletizing the material from the drying step; andshipping the pelletized material to a second location;at the second location, recovering a cellulosic solids product from the pelletized material; andcontacting the cellulosic solids so isolated with a strong mineral acid to hydrolyze the same and provide a hexose product or stream.2. A method according to claim 1 , wherein the cellulosic solids product is recovered from the pelletized material by solvent washing the pelletized material in one or more iterations with filtration claim 1 , whereby the at least partly depolymerized hemicellulosic and lignin materials from the pelletized material are separated together from the remaining cellulosic solids.3. A method according to claim 2 , further comprising claim 2 , in one or more iterations claim 2 , washing the at least partly depolymerized hemicellulosic and lignin materials with filtering to separate water-insoluble lignin solids from water-soluble hemicellulosic materials.4. A method according to claim 1 , wherein the at least partly depolymerized ...

System and Process for Refining Sugar

A system and process for refining raw sugar, comprising a melting unit configured to receive the raw sugar and an eluent to produce a melt liquor, a decolorization unit configured to receive the melt liquor and to produce a fine liquor, a crystallization unit configured to fractionate high-purity crystalline sucrose from the fine liquor and to provide a run-off syrup, a softening unit configured to receive the run-off syrup to produce a softened syrup, at least one separation unit configured to receive the softened syrup to produce a low-invert sucrose product, and a recycle line configured to relay the low-invert sucrose product from the at least one separation unit to the melting unit.

Pre-Treatment of Cellulosic Material

A method of pre-treating a cellulosic material before hydrolysis is provided. The method comprises the steps of: impregnating the cellulosic material with a reactive water-soluble gas, such as sulphur dioxide (SO) or carbon dioxide (CO), in an impregnation chamber to obtain impregnated material; and heating the impregnated material to obtain pre-treated material, wherein the cellulosic material is compressed right before or when it is transferred to the impregnation chamber. A corresponding system is also provided. 1. Method of pre-treating a cellulosic material before hydrolysis , comprising the steps of:{'sub': 2', '2, 'a) impregnating the cellulosic material with a reactive water-soluble gas, such as sulphur dioxide (SO) or carbon dioxide (CO), in an impregnation chamber to obtain impregnated material; and'}b) heating the impregnated material to obtain pre-treated material, wherein the cellulosic material is compressed right before or when it is transferred to the impregnation chamber.2. Method according to claim 1 , wherein the pressure in the impregnation chamber is 0.5-15 bar claim 1 , such as 0.5-10 bar claim 1 , such as 0.5-5.0 bar claim 1 , such as 0.7-3.0 bar claim 1 , such as 0.8-1.5 bar.3. Method according to or claim 1 , wherein temperature of the impregnation is 5-120° C.4. Method according to any one of the previous claims claim 1 , wherein the impregnation chamber contains gaseous sulphur dioxide (SO(g)) or carbon dioxide (CO(g)).5. Method according to any one of the previous claims claim 1 , wherein SOis employed.6. Method according to claim 5 , wherein the pressure in the impregnation chamber is 0.5-10 bar claim 5 , such as such as 0.5-5.0 bar claim 5 , such as 0.7-3.0 bar claim 5 , such as 0.8-1.5 bar.7. Method according to or claim 5 , wherein 0.1-10% (w/w) SOis added per dry matter of cellulosic material.84. Method according to any one of - claims 1 , wherein COis employed.9. Method according to claim 8 , wherein the pressure in the impregnation ...

METHOD OF TREATING ETHANOL PRODUCTION BYPRODUCTS

A method of treating ethanol production byproduct is provided by treating wet distillers grain or stillage with a solution containing at least one α-hydroxysulfonic acid to produce at least one fermentable sugar containing product. Fermentable sugar useful for the production of biofuels or ethanol can be produced from such methods. The α-hydroxysulfonic acid can be easily removed from the product and recycled. 1. A method of treating ethanol production byproduct comprising: (a) providing a wet distillers grain; and (b) contacting the wet distillers grain with a solution containing at least one α-hydroxysulfonic acid thereby hydrolyzing the wet distillers grain to produce at least one fermentable sugar containing product.2. The method of further comprising (c) removing the α-hydroxysulfonic acid from the product by heating and/or reducing pressure to produce an acid-removed product containing at least one fermentable sugar substantially free of the α-hydroxysulfonic acid.3. The method of further comprising recycling the removed α-hydroxysulfonic acid to step (b) as components or in its recombined form.4. The method of further comprising fermenting the acid-removed product thereby producing at least one alcohol.5. The method of further comprising hydrolyzing the acid-removed product.6. The method of further comprising fermenting the thus-hydrolyzed product thereby producing at least one alcohol.7. The method of wherein the α-hydroxysulfonic acid is present in an amount of from about 1% wt. to about 55% wt. claim 1 , based on the solution.8. The method of wherein the α-hydroxysulfonic acid is produced from a carbonyl compound or a precursor to a carbonyl compound with sulfur dioxide and water.9. The method of wherein the α-hydroxysulfonic acid is in-situ generated.10. The method of wherein step (b) is carried out at a temperature within the range of about 50° C. to about 150° C. and a pressure within the range of 1 barg to about 10 barg.11. A method comprising: (a) ...

METHOD FOR TREATING, PRESSING AND WASHING BIOMASS

A method to process cellulosic material in a treatment vessel including: introducing the cellulosic material to a processing chamber of the vessel; adding heat energy or pressure to the vessel to hydrolyze the cellulosic material in the processing chamber and dissolve hemi-cellulosic from the cellulosic material; compressing the cellulosic material in the processing chamber; extracting the dissolved hemi-cellulosic material through a screen from the processing section; draining the extracted hemi-cellulosic material from the vessel; and discharging the cellulosic material from the vessel separately from the extracted hemi-cellulosic material. 1. A method to process cellulosic material in a treatment vessel comprising:introducing the cellulosic material to a processing chamber of the vessel;adding heat energy or pressure to the vessel to hydrolyze the cellulosic material in the processing chamber and dissolve hemi-cellulosic from the cellulosic material;compressing the cellulosic material in the processing chamber;extracting the dissolved hemi-cellulosic material through a screen from the processing section during or after the compression of the cellulosic material;draining the extracted hemi-cellulosic material from the vessel; anddischarging the cellulosic material from the vessel separately from the extracted hemi-cellulosic material.2. The method of wherein the step of compressing is performed with a pressing device advancing in the vessel to reduce a volume of the processing section3. The method of further comprising crumbling the cellulosic material after being compressed.4. The method of wherein the crumbling step is performed using a mixer in the vessel.515. The method of wherein the addition of heat energy or pressure includes injection to the vessel of steam at a pressure of at least . bar gauge.6. The method of wherein the discharging of the cellulosic material includes discharging the material to a high pressure reactor.7. The method of further comprising ...

FIBER-CONTAINING CARBOHYDRATE COMPOSITION

A food product comprises an oligosaccharide composition that is digestion resistant or slowly digestible. The oligosaccharide composition can be produced by a process that comprises producing an aqueous composition that comprises at least one oligosaccharide and at least one monosaccharide by saccharification of starch, membrane filtering the aqueous composition to form a monosaccharide-rich stream and an oligosaccharide-rich stream, and recovering the oligosaccharide-rich stream. Alternatively, the oligosaccharide composition can be produced by a process that comprises heating an aqueous feed composition that comprises at least one monosaccharide or linear saccharide oligomer, and that has a solids concentration of at least about 70% by weight, to a temperature of at least about 40° C., and contacting the feed composition with at least one catalyst that accelerates the rate of cleavage or formation of glucosyl bonds for a time sufficient to cause formation of non-linear saccharide oligomers, wherein a product composition is produced that contains a higher concentration of non-linear saccharide oligomers than linear saccharide oligomers. 1. A carbohydrate composition comprising linear saccharide oligomers and non-linear saccharide oligomers , a sugar content of from about 5% to about 25% on a dry solids basis , a content of higher molecular weight polysaccharides sufficiently low such that the carbohydrate composition has a viscosity of less than about 16 ,000 cP at 100° F. and 75% dry solids , and from about 10% to about 70% fiber on a dry solids basis.2. The carbohydrate composition of claim 1 , comprising about 25 to about 40% fiber on a dry solids basis.3. The carbohydrate composition of claim 1 , wherein the carbohydrate composition has a DE of from about 23 to about 30.4. The carbohydrate composition of claim 1 , comprising about 10% to about 17% by weight sugar on a dry solids basis.5. The carbohydrate composition of claim 1 , wherein the carbohydrate ...

SOLUBLE SUGARS PRODUCED ACCORDING TO A PROCESS OF NON-AQUEOUS SOLID ACID CATALYZED HYDROLYSIS OF CELLULOSIC MATERIALS

The presently disclosed and/or claimed inventive concept(s) relates generally to processes for the non-aqueous hydrolysis of cellulose-containing material, and, more particularly but without limitation, to processes for the non-aqueous hydrolysis of cellulose-containing material into soluble sugars using a solid acid material as a catalyst. Further, the presently disclosed and/or claimed inventive concept(s) relates to non-aqueous and/or powdered soluble sugars and reaction products containing such non-aqueous and/or powdered soluble sugars produced according to a non-aqueous hydrolysis of cellulose-containing material using a solid acid material as a catalyst. 1. A reaction product produced by a non-aqueous hydrolysis reaction of a cellulose-containing material and a solid acid material.2. A method for the production of a reaction product , comprising the step of hydrolytically reacting a solid acid material and a cellulose-containing material in a non-aqueous environment for a period of time to sufficient to produce the reaction product.3. The reaction product of claim 1 , wherein the reaction product comprises at least 70% by weight of soluble sugars selected from the group consisting of glucose claim 1 , xylose claim 1 , and combinations thereof.4. The reaction product of claim 2 , wherein the reaction product comprises at least 70% by weight of soluble sugars selected from the group consisting of glucose claim 2 , xylose claim 2 , and combinations thereof. The present application is a continuation-in-part of U.S. Ser. No. 12/621,741, filed Nov. 19, 2009, entitled “SOLID ACID CATALYZED HYDROLYSIS OF CELLULOSIC MATERIALS”; which claims priority to PCT/US08/082,386, filed Nov. 5, 2008; which claims priority to U.S. Ser. No. 11/935,712, filed Nov. 6, 2007, now issued as U.S. Pat. No. 8,062,428; the entire contents of each of which is hereby expressly incorporated herein by reference. The present application also claims benefit under 35 U.S.C. 119(e) of U.S. ...

PRODUCTION OF FERMENTABLE SUGARS AND LIGNIN FROM BIOMASS USING SUPERCRITICAL FLUIDS

Methods are disclosed for the continuous treatment of biomass comprising a pretreatment step, wherein said biomass is contacted with a first supercritical, near-critical, or sub-critical fluid to form a solid matrix and a first liquid fraction; and a hydrolysis step, wherein said solid matrix formed in said pretreatment step is contacted with a second supercritical or near-supercritical fluid to produce a second liquid fraction and a insoluble lignin-containing fraction. Also disclosed are apparatuses for the continuous conversion of biomass comprising a pretreatment reactor and a hydrolysis reactor associated with said pretreatment reactor. 1. A method for the continuous treatment of biomass comprising: [{'sub': '2', 'wherein said first supercritical, near-critical, or sub-critical fluid comprises water and, optionally, CO; and'}, {'sub': 1', '5, 'wherein said first supercritical, near-critical, or sub-critical fluid is substantially free of C-Calcohol; and'}], 'a pretreatment step, wherein said biomass is contacted with a first supercritical, near-critical, or sub-critical fluid to form a solid matrix and a first liquid fraction;'} [{'sub': '2', 'wherein said second supercritical or near-critical fluid comprises water and, optionally, CO; and'}, {'sub': 1', '5, 'wherein said second supercritical or near-critical fluid is substantially free of C-Calcohols.'}], 'a hydrolysis step, wherein said solid matrix is contacted with a second supercritical or near-critical fluid to produce a second liquid fraction and an insoluble lignin-containing fraction;'}2. The method of claim 1 , wherein at least one of said first supercritical claim 1 , near-critical claim 1 , or sub-critical fluid and said second supercritical or near-critical fluid comprises less than about 10% carbon dioxide.3. The method of claim 1 , wherein said pretreatment step occurs at a temperature and pressure below the critical point of at least one component of said first supercritical claim 1 , near- ...

METHOD FOR THE ACID-CATALYZED DEPOLYMERIZATION OF CELLULOSE

A method for the acid-catalyzed depolymerization of cellulose comprises a mechanical treatment of cellulose in the presence of an inorganic and/or organic acid. The catalytic conversion of cellulose into water-soluble products is virtually completely achieved in that celluoligomers, cellubiose, glucose and glycerol are obtained without significant byproduction. 1. A method for the acid-catalyzed depolymerization of cellulose , said method comprising mechanically treating cellulose-containing material in the presence of an inorganic and/or organic acid in a catalytic amount , wherein the mechanically treating the cellulose with an acid is preceded by treating the cellulose with a mixture of said acid in a solvent and removing the solvent before the mechanically treating whereby the mechanically treating comprises grinding wherein the millbase is comminuted using grinding media.2. The method as claimed in claim 1 , wherein the acid has a pKa value of −14 to 2.3. The method as claimed in claim 1 , wherein the inorganic acid is selected from sulfuric acid claim 1 , hydrochloric acid claim 1 , phosphoric acid claim 1 , nitric acid claim 1 , haloalkanecarboxylic acids claim 1 , phosphotungstic acid and mixtures thereof4. The method as claimed in claim 1 , wherein the organic acid is selected from benzenesulfonic acid claim 1 , p-toluenesulfonic acid claim 1 , nitrobenzenesulfonic acids claim 1 , 2 claim 1 ,4 claim 1 ,6-trimethylbenzenesulfonic acid claim 1 , or derivatives thereof claim 1 , methanesulfonic acid claim 1 , maleic acid claim 1 , oxalic acid claim 1 , haloalkanecarboxylic acids and mixtures thereof.5. The method as claimed in claim 1 , wherein the inorganic acid is used in an amount of 0.0001 to 6.2 mmol per g of cellulose-containing material.68-. (canceled)9. The method as claimed in claim 5 , wherein a mill is used claim 5 , and the mill is selected from swing mills claim 5 , stirred mills claim 5 , stirred-media mills and ball mills.10. (canceled)11. The ...

PROCESS FOR PRODUCING BIO-BASED PRODUCT FROM STRAW HEMICELLULOSE AND FULLY UTILIZING THE COMPONENTS THEREOF

Provided is a process for producing biomass-based product from straw hemicellulose and utilizing the components thereof thoroughly. Steam-explosion and acid-hydrolysis are combined in the pre-treatment of straw in the process, thus a higher concentration of a sugar liquid can be obtained, and furfural and acetic acid can be recovered. The hemicellulose obtained by the pre-treatment can be used directly as ferment materials for producing butanol, succinic acid, butylene glycol, lactic acid, hydrogen and firedamp, which reduces the cost of these biomass-based products. The cellulose and lignin obtained by extracting the straw with an alkaline solution can produce products, such as sodium hydroxymethyl cellulose etc. In the process, all components in the straw can be utilized thoroughly and waste and pollutant will not be produced. 110.-. (canceled)11. A process for producing a bio-based product from straw hemicellulose and fully utilizing the components thereof , comprising the steps of:1) pretreating straw, wherein the straw is soaked in water, wherein the mass ratio of straw to water is from 1:1 to 1:3, the a soaking temperature is from 15° C. to 90° C., and the soaking period is from 10 mins to 60 mins;2) conducting steam explosion, wherein the straw soaked in step 1) is fed into a steam-explosion tank, and maintained under a steam-explosion pressure for a steam-explosion period; then the steam-exploded straw material is released, wherein the steam-explosion pressure is from 0.3 MPa to 2.0 MPa, preferably 0.5 to 1.0 MPa, and the pressure maintenance period is from 1 min to 10 mins;3) performing an acid treatment, wherein the steam-exploded straw material obtained in step 2) is fed into an acid-hydrolysis tank pre-filled with a 0.8 to 1.6% dilute acid and subjected to acid hydrolysis to generate a hydrolyzed material, wherein in the acid-hydrolysis tank, the mass ratio of the steam-exploded straw to the dilute acid is from 1:2 to 1:7, the reaction temperature is ...

SACCHARIFICATION OF LIGNOCELLULOSIC BIOMASS

An efficient process for saccharifying lignocellulosic biomass in concentrated aqueous solutions of certain bromine salts, particularly LiBr and CaBr. Real lignocellulose biomass, such as corn stover, switchgrass, waste paper, hardwood, and softwood, can be hydrolyzed without the need for any prior pretreatment. Complete saccharification of both cellulose and hemicellulose is achieved within 5-200 min at temperatures ranging from about 100 to about 160° C. Residual lignin is readily separated from product sugars by filtration or centrifugation and can be used to prepare beneficial coproducts. The bromine salt can be recovered and separated from product sugars (predominantly monosaccharides) by any art-known method and in particular solvent extraction, anti-solvent precipitation, ion-exclusion chromatography and/or ion-exchange chromatography can be employed. Hydrolysis product containing sugars can be employed for in fermentation for the production of value added products or useful fuels. 1. A method for solubilizing and/or hydrolyzing lignocellulosic material which comprises the step of contacting the lignocellulosic material with an aqueous solution of a bromine salt wherein the bromine salt is present in the solution at a concentration of 40-80% by weight of the solution at temperatures ranging from 100-160° C.2. The method of wherein the aqueous solution further comprises acid at a concentration of 1M of less.3. The method of wherein the acid concentration is less than 0.5M.4. The method of wherein the acid is an inorganic acid.5. The method of wherein the acid is HCl or HSO.6. The method of wherein the bromine salt is LiBr or CaBr.7. The method of wherein the concentration of bromine salt ranges from 55 to 65% by weight.8. The method of wherein the temperatures range from 100 to 130° C.9. The method of wherein the volume:weight ratio of solution to lignocellulosic material ranges from 10:1 to 1:1.10. A method for obtaining sugars from lignocellulosic materials ...

CONTINUOUS OR SEMI-CONTINUOUS PROCESS FOR TREATING BIOMASS TO PRODUCE MATERIALS USEFUL FOR BIOFUELS

Fermentable sugar useful for the production of biofuels is produced from biomass in a continuous or semi-continuous manner by providing pumpable biomass. 2. The process of wherein the α-hydroxysulfonic acid is present in an amount of from about 1% wt. to about 55% wt. claim 1 , based on the solution.3. The process of wherein the biomass solution contains greater than about 5 wt % of fermentable sugar.4. The process of wherein the biomass content in the biomass solution is less than about 20 wt %.5. The process of wherein the biomass content in the biomass solution is less than about 15 wt %.6. The process of wherein the biomass content in the biomass solution is about 10 wt % or less.7. The process of wherein the separation of step (d) is by centrifugal force.8. The process of wherein the separation of step (d) is by filtration.9. The process of wherein the separation of step (d) is by decantation.10. The process of further separating a C5 stream from the liquid stream.11. The process of wherein the hexose content of the wet solid stream is greater than about 0.5 wt % based on the wet solid stream.12. The process of wherein the wet solid stream contains less than 0.5 wt % furfural.13. The process of wherein the wet solid stream contains less than 0.2 wt % furfural.14. The process of wherein the α-hydroxysulfonic acid is produced from (a) a carbonyl compound or a precursor to a carbonyl compound with (b) sulfur dioxide or a precursor to sulfur dioxide and (c) water.15. The process of wherein the α-hydroxysulfonic acid is in-situ generated.16. The process of wherein the biomass is contacted with the α-hydroxysulfonic acid at a temperature of 120° C. or less.17. The process of wherein the α-hydroxysulfonic acid is produced from (a) a carbonyl compound or a precursor to a carbonyl compound with (b) sulfur dioxide or a precursor to sulfur dioxide and (c) water.18. The process of wherein the α-hydroxysulfonic acid is in-situ generated.19. The process of wherein the at ...

Centrifuge Separator

Described herein is a centrifuge separator for separating a mixture of an immiscible solid and liquid, particularly where the solid has a lower specific gravity (i.e. is lighter) than the liquid. Methods of use and a rotary seal are also described herein. 1. A centrifuge separator including:a mounting portion that releasably retains a centrifuge bowl in either stationary or spinning motion about at least two mounting points;a centrifuge bowl spindled between the mounting points with a longitudinal spin axis of the centrifuge bowl being in an approximately horizontal direction with one distil end of the centrifuge bowl inclined 0-30 degrees higher than the opposing distil end of the centrifuge bowl; andat least one inlet to the centrifuge bowl through which raw material may pass and at least one outlet from the centrifuge bowl through which a separated liquid product and/or separated solid product may pass.2. The centrifuge separator as claimed in wherein the centrifuge separator includes at least one cammed latch located on at least one end of the centrifuge bowl that allows a seal between the centrifuge bowl and an end cover to be opened when the cammed latch is actuated allowing the centrifuge bowl to be emptied of separated liquid product while the centrifuge bowl remains spinning.3. The centrifuge separator as claimed in wherein the centrifuge separator has one cammed latch located approximate the at least one outlet from the centrifuge bowl.4. The centrifuge separator as claimed in wherein the at least one cammed latch has the action of retaining the centrifuged bowl in a closed position during spinning via an over centre lever arrangement thereby creating a holding force between the at least two mounting points.5. The centrifuge separator as claimed in wherein the mounting portion includes a cradle adjacent the at least one outlet that lifts and cradles the centrifuge bowl and the outlet distil end of the centrifuge separator is opened and retains the ...

Process and equipment for sugar crystallization by controlled cooling

A process is proposed for crystallizing, by progressively cooling, in multiple stages arranged in series in a crystallization vessel ( 10 ), a descending continuous flow of a saturated sucrose solution at a temperature from about 78° to about 120° C., each stage maintaining the sucrose solution being crystallized at a predetermined temperature, until reaching a temperature from about 25 to 40° C., obtaining substantially pure sucrose crystals. A suspension containing sugar seeds is introduced in the crystallizing equipment, in the first stage, jointly with the saturated sucrose solution of 1.05-1.15. In another embodiment of the invention, the saturated solution is fed and its temperature is controlled, already in the first stage of the vessel ( 10 ), to obtain a supersaturation between 1.05 and 1.15, inducing the formation of small crystals used as crystallization seeds.

SYSTEM COMPRISING A PUMP ATTACHED TO A TANK CASING FOR MIXING A FLUID

The disclosure extends to systems, methods, and devices for mixing a fluid. The system comprises a tank conduit suspended in a tank for receiving a mixture comprising a liquid, wherein the tank holds the mixture. The system comprises a rigid casing configured to surround the tank and a pump attached to the rigid casing. The system includes a suction inlet and a discharge outlet attached to the pump, wherein the pump creates a negative pressure that draws the mixture into the pump through the suction inlet and the pump creates a positive pressure that dispels the mixture out of the pump through the discharge outlet. 1. A system for mixing a fluid , comprising:a tank conduit suspended in a tank from a top of the tank for receiving a mixture comprising a liquid, wherein the tank holds the mixture;a rigid casing comprising a plurality of sides configured to surround the tank; anda pump attached to the rigid casing, the pump comprising a suction inlet and a discharge outlet which is suspended in the tank from the top of the tank, wherein the pump creates a negative pressure that draws the mixture into the pump through the suction inlet and the pump creates a positive pressure that dispels the mixture out of the pump through the discharge outlet;wherein the tank conduit is in fluid communication with the suction inlet such that the mixture flows through the tank conduit and the suction inlet when drawn into the pump; andwherein the mixture is discharged from the pump into the tank through the discharge outlet.2. The system of claim 1 , further comprising an external fluid inlet attached to the rigid casing for receiving the liquid claim 1 , wherein the external fluid inlet is in fluid communication with the tank conduit.3. The system of claim 2 , further comprising a three-way valve in fluid communication with the external fluid inlet claim 2 , the suction inlet claim 2 , and the tank conduit.4. The system of claim 3 , wherein the three-way valve comprises a first ...

MAPLE OR BIRCH WATER EVAPORATOR SYSTEM

A system for producing maple syrup or birch syrup from maple or birch water, comprising an evaporating pan under controlled pressure, a condenser immersed in maple or birch water in the evaporating pan, and a compressor, pressurizing vapor generated by evaporation of maple or birch water in the evaporating pan, the condenser directing the pressurized vapor provided by the compressor to the maple or birch water within the evaporating pan, thereby further evaporating the maple or birch water and further generating vapor. 1. A system for producing maple syrup or birch syrup from maple or birch water , comprising:an evaporating pan under controlled pressure;a condenser immersed in maple or birch water in said evaporating pan; anda compressor, pressurizing vapor generated by evaporation of maple or birch water in said evaporating pan;wherein said condenser directs the pressurized vapor provided by said compressor to the maple or birch water within the evaporating pan, thereby further evaporating the maple or birch water and further generating vapor.2. The system of claim 1 , comprising an auxiliary heating unit claim 1 , said auxiliary heating unit first bringing the maple or birch water to its boiling temperature so as to first generate vapor needed to start the compressor.3. The system of claim 1 , comprising a water nozzle before an inlet to said compressor.4. The system of claim 1 , comprising temperature controllers claim 1 , said temperature controllers monitoring a temperature difference between the maple or birch water within the evaporating pan and walls of the condenser.5. The system of claim 1 , comprising a flow controller claim 1 , said flow controller monitoring the flow of maple or birch water within the evaporating pan.6. The system of claim 1 , wherein the surface of the condenser is selected according to a target heat flux.7. The system of claim 1 , comprising non condensable gases evacuation upstream of the compressor.8. The system of claim 1 , wherein ...

Potash Processing with Mechanical Vapor Recompression

A potash-extraction system and method for extracting potash from a brine containing potash without the use of water-consuming evaporation ponds or additional chemicals is disclosed. The potash processing system uses a mechanical-vapor recompression (“MVR”) cycle to separate salt and then potash from a sylvinite brine containing salt and potash. In embodiments, the latent heat recovered from condensing vapor may be used to boil the brine to precipitate some salt and remove some water (in the form of water vapor) from the brine. The remaining potash-concentrated brine may then be cooled to precipitate potash from the solution. The precipitated potash may then be further processed for final use. 1. A potash processing system , the system comprising:a first-stage and a second-stage crystallizer;a concentrator; and receive a sylvinite brine comprising potash, salt, and water from a sylvinite brine source;', 'boil the sylvinite brine in the concentrator to produce precipitated salt, water vapor, and potash-concentrated brine;', 'cool the potash-concentrated brine in the first-stage crystallizer to produce first-stage precipitated potash and saturated-potash brine; and', 'cool the saturated-potash brine in the second-stage crystallizer to produce second-stage precipitated potash and cooled saturated-potash brine., 'wherein the potash processing system is configure to2. The potash processing system of claim 1 , wherein the potash processing system is further configured to return to the sylvinite brine source more than 80% of the water in the sylvinite brine received from the sylvinite brine source.3. The potash processing system of claim 1 , wherein the potash processing system is further configured to capture from the sylvinite brine more than 80% of the potash in the sylvinite brine received from the sylvinite brine source.4. The potash processing system of claim 3 , wherein the potash processing system is configured to recycle the cooled saturated-potash brine back in ...

PROCESS FOR PURIFYING BEET JUICE

The present invention relates to a process for purifying beet sugar juice and more particularly sugar juice obtained by pressing beets. It also relates to the purified juice and to the uses thereof, in particular as a fermentation substrate and for preparing granulated sugar. The purification process according to the invention comprises a step of passing the juice to be treated through a cellulose-fibre-based pre-layer. This process can be improved when the juice to be treated comprises between 0.1% and 4% of cellulose fibres. 1. A process for purifying beet sugar juice , comprising a step of passing said juice through a filtration precoat , characterized in that said juice comprises cellulose fibers at a content of between 0.1% and 4% by weight.2. The process as claimed in claim 1 , characterized in that the cellulose fiber content is preferentially between 0.2% and 3% by weight.3. The process as claimed in either of the preceding claims claim 1 , characterized in that the filtration is carried out by means of a scraped precoat rotary filter.4. The process as claimed in claim 3 , characterized in that the precoat consists of 100% of cellulose fibers.5. The process as claimed in one of to claim 3 , characterized in that the filtration is frontal.6. The process as claimed in one of the preceding claims claim 3 , characterized in that the filtration step is preceded by a centrifugation step. The present invention relates to a process for purifying beet sugar juice and more particularly sugar juice obtained by pressing beets. It also relates to the purified juice and to the uses thereof, in particular as a fermentation substrate and for preparing granulated sugar.Beet sugar juices are generally obtained by means of an extraction process denoted “diffusion extraction”. This process can be summarized as follows: the sugar beets are first of all washed and then chopped into cossettes before passing into a large-capacity extractor in which hot water circulates ...

Method to liquefy biomass

A method of liquefying biomass. The method includes the steps of contacting biomass with a solution comprising an acyl halide and an acid; and then contacting the biomass with a reductant.

STIRRERS FOR CRYSTALLIZING EVAPORATOR

A stirrer for a crystallizing evaporator such a crystallizing evaporator for crystallizing sucrose from concentrated beet juice. The stirrer includes at least one active flow-conducting means selected from a group consisting of a plurality of flow-conducting propellers arranged along a shaft of the stirrer and a screw running along the shaft. 1. A stirrer for a vacuum pan , suitable for circulating a solution or suspension to be crystallized in a vessel , comprising a shaft ,a main propeller disposed in a primary mixing zone and connected to the shaft; andat least one active flow-conducting means on the shaft and upstream of the main propeller for active flow guidance of the solution or suspension, the at least one active flow-conducting means is selected from a group consisting of:1) a plurality of flow-conducting propellers each having a flow-conducting propeller diameter less than 50% of a main propeller diameter of the main propeller, the plurality of propellers arranged at a distance from each other along the shaft, and2. a screw running along the shaft, having a screw that is a diameter at most 50% of the main propeller diameter.2. The stirrer according to claim 1 , wherein the at least one active flow-conducting means is arranged directly adjacent to the primary mixing zone.3. The stirrer of in combination with the vacuum pan.4. The vacuum pan according to claim 3 , wherein the vacuum pan is designed for discontinuous operation.5. A method of using the active flow-conducting means of claim 1 , on the shaft of the stirrer to improve a mixing capacity.6. The method according to for improving the mixing capacity of the stirrer in a vacuum pan in discontinuous operation.7. The stirrer according to claim 1 , wherein the at least one active flow-conducting means comprises the plurality of flow conducting propellers.8. The stirrer according to claim 1 , wherein the at least one active flow-conducting means comprises the screw. This application is a 371 U.S. National ...

RAW SUGAR AND ETHANOL PRODUCTION METHOD USING SELECTIVE FERMENTATION

A method for producing raw sugar and ethanol which includes the steps of: heating and clarifying a plant origin sugar juice; concentrating the clear sugar juice so that the Brix value of the clear sugar juice is 15 to 50%; cooling the syrup to a fermentation temperature; fermenting the syrup, thereby selectively converting the saccharide components other than sucrose in the syrup into ethanol; and concentrating the fermented solution. 17-. (canceled)8. A method for producing raw sugar and ethanol comprising the steps of:heating and clarifying a plant-origin sugar juice;concentrating the clear sugar juice so that Brix value of the clear sugar juice is 15 to 40%;cooling the syrup to a fermentation temperature;fermenting the syrup, thereby selectively converting the saccharide components other than sucrose in the syrup into ethanol;concentrating the fermented solution; andcrystallizing sugar from the concentrated fermented solution.9. A method for producing raw sugar and ethanol comprising the steps of:heating and clarifying a plant-origin sugar juice;introducing the clear sugar juice into a multiple-effect evaporator tube;concentrating the clear sugar juice so that Brix value of the clear sugar juice is 15 to 40% by letting the clear sugar juice pass through an evaporator tube placed in the first position of the multiple-effect evaporator tube and thereafter drawing the clear sugar juice before introducing the clear sugar juice into an evaporator tube placed in the last position of the multiple-effect evaporator tube;cooling the syrup to a fermentation temperature;fermenting the syrup, thereby selectively converting the saccharide components other than sucrose in the syrup into ethanol;heating the fermented solution to a concentration temperature;concentrating the fermented solution by letting the fermented solution pass through an evaporator tube placed in the next position of the evaporator tube from which the syrup is drawn; andcrystallizing sugar from the ...

NOVEL SUCROSE UNASSIMILATING FLOCCULENT YEAST

An object of the present invention is to provide a sucrose unassimilating yeast which has a flocculation ability and has much of a proven performance of food production. The present invention pertains to a yeast strain expressed by accession number: NITE BP-1587. 1. A yeast strain expressed by accession number: NITE BP-1587.2. A yeast strain expressed by accession number: NITE BP-1588.3. (canceled)4. The yeast strain according to claim 1 , wherein the yeast is employed for a method of producing sugar and ethanol comprising a step of fermenting sugar liquid derived from a plant with yeast.5. The yeast strain according to claim 2 , wherein the yeast is employed for a method of producing sugar and ethanol comprising a step of fermenting sugar liquid derived from a plant with yeast.6. The yeast strain according to claim 1 , wherein the yeast is employed for a method of producing sugar and ethanol comprising steps of:removing non-sugar components contained in sugar liquid derived from a plant to clarify the sugar liquid; andadding yeast to the clarified sugar liquid to carry out ethanol fermentation at a given temperature under an anaerobic condition for an appropriate length of time.7. The yeast strain according to claim 2 , wherein the yeast is employed for a method of producing sugar and ethanol comprising steps of:removing non-sugar components contained in sugar liquid derived from a plant to clarify the sugar liquid; andadding yeast to the clarified sugar liquid to carry out ethanol fermentation at a given temperature under an anaerobic condition for an appropriate length of time.8. A method of producing sugar and ethanol comprising a step of fermenting sugar liquid derived from a plant with the yeast strain according to .9. A method of producing sugar and ethanol comprising a step of fermenting sugar liquid derived from a plant with the yeast strain according to .10. A method of producing sugar and ethanol comprising steps of:removing non-sugar components contained ...

CENTRIFUGAL SEPARATING ASSEMBLY

A centrifugal separating assembly for separating a fluid biological product into discrete components by centrifugation is disclosed. The assembly includes a first container defining a first cavity adapted to receive a human biological product, the first container having a circular upper wall, a cylindrical sidewall, and a concave shaped bottom wall. The assembly further includes a second container defining a second cavity adapted to receive discrete components, the second container having a convex shaped upper wall, a second cylindrical wall, and a circular bottom wall; and a tubular conduit providing fluid communication between the first cavity and the second cavity. 1. A centrifugal separating assembly for separating a fluid biological product into discrete components by centrifugation , the assembly comprising: a circular upper wall,', 'a first cylindrical wall extending downwardly from a circumferential edge of the circular upper wall, and', 'a concave shaped bottom wall extending inwardly and downwardly from a circumferential edge of the first cylindrical wall, the concave shaped bottom wall terminating at a distal end of the first container and the distal end of the first container defining a first tubular conduit receiving aperture;, 'a first container defining a first cavity adapted to receive and hold the fluid biological product, the first container having a convex shaped upper wall extending upwardly and inwardly from an upper circumferential edge of a second cylindrical wall and terminating at a distal end of the second container, the distal end of the second container defining a second tubular conduit receiving aperture,', 'the second cylindrical wall extending downwardly from a circumferential edge of the convex shaped upper wall, and', 'a circular bottom wall extending inwardly from a lower circumferential edge of the second cylindrical wall; and, 'a second container defining a second cavity adapted to receive discrete components of the fluid ...

DISSOLUTION METHOD

A method that can efficiently dissolve a water-soluble component contained in a gas with smaller energy consumption is provided. A mist is produced from a liquid. The mist and carrier air is mixed to produce mist-containing air. A solution gas and the mist-containing air are supplied to a static mixer. The solution gas and the mist-containing are mixed by using the static mixer. The liquid mist is brought in contact with the solution gas to dissolve a water-soluble component that is contained in the solution gas into the liquid mist. The liquid mist that contains the water-soluble component dissolved aggregates and produces a solution that contains the water-soluble component dissolved. 1. A dissolution method comprising:oscillating a liquid at an ultrasonic frequency to produce a liquid column;forcedly blowing air to the liquid column produced to separate a mist of the liquid from the liquid column whereby producing mist-containing air;supplying a soluble gas and the mist-containing air to a static mixer;mixing the soluble gas and the mist-containing by using the static mixer;bringing the liquid mist in contact with the soluble gas to dissolve a water-soluble component that is contained in the soluble gas into the liquid mist; andaggregating the liquid mist that contains the water-soluble component dissolved to produce a solution that contains the water-soluble component dissolved.2. A dissolution method comprising:spraying a liquid by using a spray device;exposing a sprayed mist of the liquid to an electric field and mixing the mist, and carrier air to produce mist-containing air;supplying a soluble gas and the mist-containing air to a static mixer;mixing the soluble gas and the mist-containing by using the static mixer;bringing the liquid mist in contact with the soluble gas to dissolve a water-soluble component that is contained in the soluble gas into the liquid mist; andaggregating the liquid mist that contains the water-soluble component dissolved to produce ...

MAPLE TREE SAP REVERSE OSMOSIS DEVICE

A maple sap reverse osmosis device has a support rack configured and sized to rest atop a tank. The support rack supporting a reverse osmosis device. The reverse osmosis device has a pump line and a dump line both located within the tub. The pump line being located at an upper region of the tank. A pumping means to pump the maple sap from the pump line. The pumping means pushing maple sap through an osmosis membrane. The dump pipe purging concentrate resulting from sap not passing through the osmosis membrane into the deepest region of the tub. 1. A maple sap reverse osmosis device comprising:a support rack configured and sized to rest atop a tank;the support rack supporting a reverse osmosis device;the reverse osmosis device has a pump line and a dump line both located within the same tank;the pump line being located at an upper region of the tank;a pumping means to pump the maple sap from the pump line;the pumping means pushing maple sap towards an osmosis membrane;a recirculating pump to process the sap inside a module;the dump pipe purging concentrate, resulting from sap that has passed through the module, into a deepest region of the tank.2. A maple sap reverse osmosis device as in wherein:the pumping means is a feed pressure pump consisting of a rotary vane pump.3. A maple sap reverse osmosis device as in wherein:the pumping means is a feed pressure pump capable of sustaining a pressure of between 200 and 270 psi.4. A maple sap reverse osmosis device as in wherein:the pump line has a float so that it pumps only sap water located at the top of the sap contained in the tank, which determines the upper region of the tank.5. A maple sap reverse osmosis device as in having a method of operation consisting in the steps of:the pumping means takes the sap from the tank and brings the pressure between 200 to 270 psi at a volume of 1.66 gallons per minute;the pressure of between 200 to 270 psi pushes the sap through a 5 to 10 micron filter located between the feed pump ...

COOLING CRYSTALLIZER AND SUGAR CRYSTALLIZATION METHOD

The invention relates to a cooling crystallizer () for saccharose magma in a vertically oriented container () which has an upper inlet () for supplying magma and a lower outlet () for discharging magma, comprising multiple cooling blocks () which are mutually spaced in a vertical direction. A heat carrier fluid flows through the cooling blocks (), and the cooling blocks are coupled to a heat exchanger in order to dissipate heat from the magma, wherein multiple cooling blocks () are combined to form a cooling packet (), and the cooling packets () are designed as separate cooling circuits with separate heat exchangers (). 1. A cooling crystallizer for sucrose magma in a vertically oriented container , which has an inlet at a top of the vertically oriented container for feeding in the sucrose magma and an outlet at a bottom of the vertically oriented container for discharging the sucrose magma , comprising:a plurality of cooling blocks which are vertically spaced apart from one another, wherein each of the cooling blocks of the plurality of cooling blocks is configured for a heat transfer fluid to flow therethrough,a plurality of heat exchangers, wherein at least some of the plurality of heat exchangers are coupled to at least some of the plurality of cooling blocks in order to dissipate heat from the sucrose magma,wherein a plurality of cooling packs are formed from cooling blocks of the plurality of cooling blocks being combined together, wherein each of the cooling packs of the plurality of cooling packs are configured as separate cooling circuits with separate heat exchangers of the plurality of heat exchangers.2. The cooling crystallizer as claimed in claim 1 , wherein the plurality of cooling packs are configured be vertically separate.3. The cooling crystallizer as claimed in wherein the plurality of cooling packs are arranged in the vertically oriented container and are configured such that a temperature difference between the sucrose magma and a respective ...

CENTRIFUGAL JUICER

A centrifugal juicer () is disclosed that can be configured to control the pulp content in the juice produced by the juicer. To this end, the centrifugal juicer comprises a pulp content selection function that controls the rotation speed of the motor driving the sieve () of the centrifugal juicer. The openings () in the sieve are dimensioned such that pulp is forced through the openings at certain rotation speeds of the motor. 1. A centrifugal juicer comprising:a food shredding element cooperating with a circular sieve comprising a plurality of openings;a motor adapted to rotate the circular sieve, wherein the motor has a variable rotation speed and said openings are dimensioned such that food pulp can be forced through said openings at certain rotation speeds of the motor; anda user interface comprising a pulp content selection function, wherein the variable rotation speed of the motor is controlled by said pulp content selection function.2. The centrifugal juicer of claim 1 , wherein the pulp content selection function is implemented as a switch that can be switched between a first position indicating juice having a lower pulp content and a second position indicating juice having a higher pulp content claim 1 , wherein the motor operates at a first speed when the switch is in the first position and operates at a second speed when the switch is in the second position claim 1 , the second speed being higher than the first speed.3. The centrifugal juicer of claim 1 , wherein the switch is a dial that can be turned between the first position and the second position.4. The centrifugal juicer of claim 1 , wherein said openings have a diameter in the range of 0.25-0.5 mm.5. The centrifugal juicer of or claim 1 , wherein said openings have a diameter of about 0.35 mm claim 1 , and wherein the second speed is in the range of 1.3-1.5 times the first speed.6. The centrifugal juicer of claim 5 , wherein the circular sieve has a diameter in the range of 110-160 mm claim 5 , ...

System And Method For Plasma Purification Prior To Mononuclear Cell Collection

A method of collecting mononuclear cells includes separating whole blood into plasma and cellular components, purifying the plasma through a plasma adsorption column to create purified plasma, combining the cellular components with the purified plasma to form a first mixture, and separating the first mixture into mononuclear cells and at least one component. Alternatively, whole blood may be flowed through an adsorption column to create purified whole blood, with the purified whole blood then being separated into mononuclear cells and at least one component. 111-. (canceled)12. A method of collecting mononuclear cells , comprising:separating whole blood into plasma and cellular components;purifying the plasma through a plasma adsorption column to create purified plasma;combining the cellular components with the purified plasma to form a first mixture; andseparating the first mixture into mononuclear cells and at least one component.13. The method of claim 12 , further comprising the step of performing extracorporeal photopheresis on the mononuclear cells claim 12 , and wherein the purified plasma contains fewer proteins claim 12 , lipids claim 12 , and/or bilirubin than does the plasma.14. The method of claim 12 , wherein the step of separating whole blood into plasma and cellular components is performed by a centrifugal separator.15. The method of claim 12 , wherein step of separating whole blood into plasma and cellular components is performed by a spinning membrane separator.16. The method of claim 12 , wherein the mononuclear cells comprise at least one of lymphocytes claim 12 , monocytes claim 12 , and stem cells.17. A method of collecting mononuclear cells claim 12 , comprising:providing an adsorption column through which whole blood is flowed to create purified whole blood; andseparating the purified whole blood into mononuclear cells and at least one component.18. The method of claim 17 , wherein the purified whole blood is separated by a centrifugal ...

SUGAR COMPOSITION

The present invention provides food grade sugar particles comprising sucrose crystals, reducing sugars and polyphenols, wherein the sugar composition comprises about 0 to 0.15 g/100 g reducing sugars and about 20 mg/100 g to about 45 mg/100 g polyphenols and the sugar particles have a glucose based glycaemic index of less than 55. 1. Food grade sugar particles comprising sucrose crystals , reducing sugars and polyphenols , wherein the sugar particles comprise about 0 to about 0.5 g/100 g reducing sugars; andabout 20 mg/100 g to about 45 mg/100 g polyphenols; andwherein the sugar particles have a glucose based glycaemic index of less than 55.2. The sugar particles of claim 1 , wherein a first proportion of the polyphenols are entrained within the sucrose crystals and a second proportion of he polyphenols is distributed on the surfaces of the sucrose crystals.3. The sugar particles of claim 2 , wherein the proportion of the polyphenols entrained within the sugar crystals is about 25% to 30% of the total polyphenol content of the sugar particles.4. A method for preparing sugar particles comprising washing massecuite to produce sugar particles claim 2 , wherein the massecuite includes sucrose crystals claim 2 , polyphenols and reducing sugars claim 2 , wherein the wash removes an amount of polyphenols and an amount of reducing sugars from the massecuite claim 2 , wherein the sugar particles comprise about 0 to 0.5 g/100 g reducing sugars and about 20 mg/100 g to about 45 mg/100 g polyphenols and wherein the sugar particles have a glucose based glycaemic index of less than 55.5. A method for preparing sugar particles according to claim 4 , wherein the wash is ceased when the sugar particles comprise 0 to 0.5 g/100 g reducing sugars and less than about 45 mg CE/100 g polyphenols and additional polyphenols are added to the sugar particles to prepare sugar comprising about 20 mg CE/100 g to about 45 mg CE/100 g polyphenols.6. A method for preparing sugar particles according ...

CRYSTALLIZATION SYSTEM AND PROCESS

A system for the crystallization of a substance to be crystallized which is dissolved in a solvent, comprising a crystallization apparatus which is flowed through by a solution to be concentrated which has the substance to be crystallized dissolved therein, and by a heating steam or a heating liquid, wherein the crystallization apparatus has at least one flow passage conducting the solution to be concentrated, at least one flow passage conducting the heating steam or the heating liquid, and at least one flow passage conducting vaporous solvent, wherein a respective flow passage conducting the solution to be concentrated is at least partly separated from a respective flow passage conducting the heating steam or the heating liquid by a steam-impermeable and liquid-impermeable wall and wherein a respective flow passage conducting the solution to be concentrated is at least partly separated from a respective flow passage conducting the vaporous solvent by a membrane wall permeable to the vaporous solvent, but not to the liquid solvent, wherein the crystallization apparatus is configured such that the solution to be concentrated is boiled in the respective flow passage conducting the solution to be concentrated and vaporous solvent produced during the boiling moves through the membrane wall into the adjacent flow passage conducting the vaporous solvent. 115-. (canceled)16. A system for the crystallization of a substance to be crystallized which is dissolved in a solvent , the system comprising a crystallization apparatus which is flowed through by a solution to be concentrated having the substance to be crystallized dissolved therein , and which is flowed through by a heating steam or a heating liquid , wherein the crystallization apparatus comprises:at least one flow passage conducting the solution to be concentrated,at least one flow passage conducting the heating steam or the heating liquid, and 'wherein a respective flow passage conducting the solution to be ...

Process for sugar production

The application relates to methods and systems for producing a sugar product. The method includes: receiving a first input in a control system representative of a pre-treatment sugar composition characteristic; receiving a second input in the control system representative of a post-treatment sugar product target specification; using the control system to determine at least one operating parameter for a centrifuge and operating the centrifuge in accordance with the at least one determined operating parameter, wherein the at least one determined operating parameter is determined from at least: the first input, the second input, and a correlation relating at least the first input and the second input to the at least one operating parameter; and treating the pre-treatment sugar composition in the centrifuge to produce a post-treatment sugar product with a characteristic that is at or nearer to the target specification than the characteristic of the pre-treatment sugar composition.

METHOD OF PRODUCING SUGAR SOLUTION

A method of producing a sugar liquid includes filtering a cellulose-derived sugar liquid through one or more separation membranes selected from the group consisting of an ultrafiltration membrane, a nanofiltration membrane and a reverse osmosis membrane and washing the separation membrane(s) after filtration with washing water containing an alkaline substance and an aromatic compound at 10° C. or more and less than 50° C. 17-. (canceled)8. A method of producing a sugar liquid comprising filtering a cellulose-derived sugar liquid through one or more separation membranes selected from the group consisting of an ultrafiltration membrane , a nanofiltration membrane and a reverse osmosis membrane and washing the separation membrane(s) after filtration with washing water containing an alkaline substance and an aromatic compound at 10° C. or more and less than 50° C.9. The method of producing a sugar liquid according to claim 8 , wherein the alkaline substance is sodium hydroxide and/or potassium hydroxide.10. The method of producing a sugar liquid according to claim 8 , wherein the aromatic compound is one or two selected from the group consisting of hydroxymethylfurfural (HMF) claim 8 , furfural claim 8 , coumaric acid claim 8 , ferulic acid claim 8 , coumaramide claim 8 , ferulamide and vanillin.11. The method of producing a sugar liquid according to claim 8 , wherein the washing water is a derived from a filtrate obtained by passing a cellulose-derived sugar liquid through a nanofiltration membrane and/or a reverse osmosis membrane.12. The method of producing a sugar liquid according to claim 8 , wherein the cellulose-derived sugar liquid is a cellulose-derived sugar liquid filtered through a microfiltration membrane.13. The method of producing a sugar liquid according to claim 8 , wherein the separation membrane is washed by cross-flow filtration of the washing water through the separation membrane(s).14. The method of producing a sugar liquid according to claim 13 , ...

SYSTEM AND METHOD FOR PLASMA PURIFICATION PRIOR TO MONONUCLEAR CELL COLLECTION

A method of collecting mononuclear cells, comprising separating whole blood into plasma and cellular components, combining the cellular components with plasma replacement fluid to form a first mixture, and separating the first mixture into mononuclear cells and at least one component. 1. A method of collecting mononuclear cells , comprising:separating whole blood into plasma and cellular components;combining the cellular components with plasma replacement fluid to form a first mixture; andseparating the first mixture into mononuclear cells and at least one component.2. The method of claim 1 , further comprising the step of performing extracorporeal photopheresis on the mononuclear cells claim 1 , and wherein the plasma replacement fluid contains fewer proteins claim 1 , lipids claim 1 , and/or bilirubin than does the plasma.3. The method of claim 1 , wherein the step of separating whole blood into plasma and cellular components is performed by a centrifugal separator.4. The method of claim 3 , furthering comprising the steps of separating the whole blood within a compartment of a separation chamber claim 3 , directing the plasma and cellular components to separate containers until separation of the whole blood is complete claim 3 , directing the first mixture into the compartment claim 3 , and separating the first mixture into mononuclear cells and at least one component in the compartment.5. The method of claim 4 , wherein the steps of separating whole blood into plasma and cellular components and separating the first mixture into mononuclear cells and at least one component take place substantially in series.6. The method of claim 3 , further comprising the steps of separating the whole blood within a first compartment of a separation chamber claim 3 , directing the plasma to a container claim 3 , directing the first mixture to a second compartment of the separation chamber claim 3 , and separating the first mixture into mononuclear cells and at least one ...

Process for Refining Impure Crystallised Sucrose

The invention relates to a process for refining impure crystallised sucrose which process comprises the application of multiple effect falling film evaporation to concentrate without crystallisation a runoff produced on centrifugation of massecuite arising from a sucrose crystallisation process. 1. A process for refining impure crystallised sucrose , the process comprising the application of multiple effect falling film evaporation to concentrate without crystallisation a runoff produced on centrifugation of massecuite arising from a sucrose crystallisation process.2. A process according to wherein the sucrose crystallisation process is a cooling crystallisation process.3. A process according to wherein the impure crystallised sucrose is derived from sugarcane.4. A process according to wherein the runoff has a Brix value of from 66 to 72 before the application of multiple effect falling film evaporation.5. A process according to wherein the runoff (syrup) has a Brix value of from 80 to 83 after the application of multiple effect falling film evaporation.6. A process according to wherein the multiple effect falling film evaporation is integrated into a single operation.7. A process according to wherein the multiple effect evaporation is a two effect claim 1 , three effect claim 1 , four effect or five effect evaporation.8. A process according to wherein a first effect of the multiple effect evaporation is achieved by supplying steam to a first evaporator at a pressure of between approximately 160 to 220 kPA absolute with corresponding vapour saturation temperatures of 113.3 to 123.3 degrees Centigrade.9. A process according to wherein the last effect of the multiple effect evaporation runs at a pressure of between approximately 10 and 30 KPa absolute corresponding to saturated vapour temperatures of between 45.8 and 69.1 degrees Centigrade.10. A process according to wherein the process includes bleeding steam for use outside the evaporator system.11. A process ...

High purity lactose

An example system for purifying a supply stream including lactose includes a clarification system configured to separate insoluble impurities from the stream to produce a clarified stream. The system includes an adsorption system fluidically coupled to the clarification system. The adsorption system includes an adsorbent resin configured to purify the clarified stream. An example technique for purifying a supply stream including lactose includes separating insoluble impurities from the supply stream to produce a clarified stream and passing the clarified stream over an adsorbent resin to produce a decolorized stream.

METHOD FOR THE PREPARATION OF HIGH TEST MOLASSES

The invention relates to a method the preparation of an inverted sugar product, called high test molasses, using novel reaction parameters. More particularly it relates to the preparation of high-test molasses using an acid wherein the loss of sugar due to use of acid and high temperature as in conventional method is eliminated. 1. A method for the preparation of high test molasses from sugarcane or sugar beet juice comprising:(a) concentrating said juice by evaporation to contain a higher amount of sucrose forming a concentrated syrup;(b) adding a desired amount of organic acid to said syrup creating a reaction mixture; and(c) treating said reaction mixture at an effective temperature for a desired time period to cause inversion of sucrose to inverted sugar forming a high test molasses product.2. The method of claim 1 , wherein said concentrated syrup comprises up to 50% by weight of sucrose.3. The method of claim 1 , wherein said organic acid is methane sulphonic acid.4. The method of claim 1 , wherein said organic acid is used between 0.1 to 1.0% by weight of concentrated syrup.5. The method of claim 1 , wherein said effective temperature ranges from about 75° C. to about 95° C.6. The method of claim 1 , wherein said desired time period ranges from about 1 hour to about 4 hours.7. The method of claim 1 , wherein efficiency of conversion of said sucrose to inverted sugar is at least 90% by weight.8. The method of claim 1 , wherein efficiency of recovery of said inverted sugar is above 90% by weight.9. The method of claim 1 , wherein said high test molasses has Brix value of at least 85°. The invention relates to a method for the preparation of an inverted sugar product, called high test molasses, using novel reaction parameters. More particularly it relates to the preparation of high-test molasses using an acid wherein the loss of sugar due to use of acid and high temperature as in conventional method is eliminated.High test molasses [HTM] is made from the ...

ADIPOSE TISSUE CENTRIFUGE AND METHOD OF USE

A centrifuge device is provided for the sizing and separation of constituents of a biologic mixture, e.g., adipose tissue. The device provides for the mechanical breaking down of the fibrous structure in the tissue by centrifugation causing the tissue to pass through a mesh element, or a sizing helix, or an extrusion element, whereupon the material is reduced to a slurry. This processed material may then be separated by centrifugation into its constituents, in order to harvest the fraction containing the multipotent cells. These multipotent cells may be utilized for various medical procedures to stimulate healing and tissue regeneration. 130.-. (canceled)31. A method for processing a biologic mixture and selectively concentrating constituents of the biologic mixture , the constituents having differing specific gravities and being stratifiable in a centrifugal field , said method comprising:a. introducing a biologic mixture comprising adipose tissue into a chamber of a centrifuge, said chamber comprising a sidewall with a tapered inner surface, a base, an annular screen having an inner surface and a first port;b. rotating said chamber about an axis to pass at least a portion of said adipose tissue through said screen, thereby morselizing the adipose tissue; and causing the biologic mixture to stratify in said chamber into at least two concentric stratified constituent layers.32. The method of claim 31 , wherein the biologic mixture comprises adipose tissue and water based liquids.33. The method of claim 31 , wherein one of the at least two concentric stratified constituent layers comprise multipotent cells.34. The method of claim 33 , further comprising the step of harvesting said multipotent cells from said centrifuge.35. The method of claim 31 , wherein the annular screen has an inner surface located at a first radial distance from the axis claim 31 , the annular screen projecting away from the base.36. The method of claim 35 , wherein the centrifuge further ...

Advanced Liquid Centrifuge Using Differentially Rotating Cylinders and Optimized Boundary Conditions, and Methods for the Separation of Fluids

Provided is an advanced liquid centrifuge using differentially rotating cylinders moveable rings at the ends thereof, as well as methods for the separation of fluids, preferably liquids. 1. An apparatus for the separation of a composition into two more fractions or parts , which apparatus comprises:an annulus for the containment of a composition, which annulus exists between a rotatable inner cylinder (IC), a rotatable outer cylinder (OC), and one or more rotatable rings (RR) which extend between the inner cylinder and the outer cylinder and particularly at or near the ends thereof, wherein each of the inner cylinder, the outer cylinder and the one or more rotatable rings are all independently mobile, preferably rotatable, with respect each other, and wherein the inner cylinder, the outer cylinder, and the one or more rotatable rings are all concentric about a central axis, which may be oriented at any angle, but is preferably horizontally, diagonally or vertically oriented.2. An apparatus according to claim 1 , wherein the apparatus further includes: drive means which are used to impart rotational motion to one or more of the inner cylinder claim 1 , the outer cylinder and the one or more rotatable rings.3. An apparatus according to which further includes: one or more liquid ports whereby the contents of the annulus may be provided and/or removed claim 2 , respectively claim 2 , to or from the apparatus and/or one or more fluid pumps and/or one or more pump controllers and/or one or more drive controllers.4. A separation method for the separation of a composition claim 2 , into two or more component fractions or parts claim 2 , which method comprises the steps of:providing the composition to an apparatus which comprises an annulus for the containment of a composition which annulus exists between an a rotatable inner cylinder (IC), a rotatable outer cylinder (OC), and one or more rotatable rings which extend between the inner cylinder and the outer cylinder, which ...

Method of preventing carbohydrate crystallization

The invented method prevents precipitation of a carbohydrate, such as trehalose, in a solution comprising mixing an effective amount of at least one antifreeze protein with the carbohydrate in the solution, wherein the antifreeze protein is described in whole or in part by one of SEQ. ID 1, SEQ. ID 2, SEQ. ID 3, and SEQ. ID 4, and wherein the antifreeze protein mass to the carbohydrate mass is between about 1:8000 and 1:30. Trehalose is a multifunctional non-reducing disaccharide, having a wide range of applications in industries (e.g., medical, pharmaceutical, and food industries). However, trehalose has a high propensity to precipitate/crystallize out of the solutions or formulations particularly at low temperatures, forming trehalose dihydrate. The invention is especially useful for improving the applications of a carbohydrate, such as trehalose, and the quality of the carbohydrate-containing products in industries by prevention the carbohydrate crystallization in formulations and products.

Tagatose production from deproteinized whey and purification by continuous chromatography

Disclosed is a process for the production of d-tagatose from deproteinized whey or whey permeate containing lactose after acid hydrolysis to provide a hydrolysate comprising 1 equivalent of d-glucose and 1 equivalent of d-galactose for each unit of lactose converted. More particularly, the invention relates to a process for the isomerization of d-galactose to d-tagatose and the use of a simplified separation scheme based on simulated moving bed (SMB) separation. The isomerization of d-galactose to d-tagatose is carried out in the presence of calcium oxide or calcium hydroxide. The process is useful for providing a simplified processing route to providing pure d-tagatose and glucose syrup as two products from lactose hydrolysate isomerate. D-tagatose is useful as a food additive, as a sweetener, as a texturizer, as a stabilizer, or as a humectant.

METHOD OF PREPARING OLIGOSACCHARIDE USING BIOMASS SUGAR AS RAW MATERIAL

The present invention discloses a method of preparing oligosaccharide using biomass sugar as raw material. The method places a biomass sugar in a quartz tubular reactor, places the quartz tubular reactor at a temperature-controlled zone of a tubular thermal conversion reactor under the protection of nitrogen gas, controls a thermal conversion time, rapidly quenches a material to obtain an oligosaccharide precursor after thermal conversion ends, then dissolves by adding pure water and purifies through an inorganic ultrafiltration membrane, and finally obtain an oligosaccharide after drying. 1. A method of preparing an oligosaccharide using a biomass sugar as raw material , the method comprises the following steps:(1) placing the biomass sugar in a quartz tubular reactor, then passing a high-purity nitrogen gas to replace air in the quartz tubular reactor, setting a temperature of a tubular thermal conversion reactor to 300° C. to 700° C., when the temperature in the tubular thermal conversion reactor reaching the set temperature and being stable, placing the quartz tubular reactor at a temperature-controlled zone of the tubular thermal conversion reactor, controlling a thermal conversion time to 10 seconds to 130 seconds, and then placing the quartz tubular reactor in a cooling liquid or air to quench, so as to obtain an oligosaccharide precursor;(2) dissolving the oligosaccharide precursor obtained in step (1) by adding a pure water, so as to obtain an oligosaccharides-rich solution;(3) purifying the oligosaccharide-rich solution obtained in step (2) through an inorganic ultrafiltration membrane, so as to obtain an oligosaccharide solution having a molecular weight within 1500;(4) drying the oligosaccharide solution obtained in step (3), so as to obtain the oligosaccharide.2. The method according to claim 1 , wherein in step (1) claim 1 , the biomass sugar is one or a plurality of monosaccharide claim 1 , disaccharide and oligosaccharide obtained by an enzymolysis ...

SYSTEMS AND METHODS FOR PRESERVING NUTRIENTS DURING THE PRODUCTION OF SYRUPS AND POWDERS FROM SUGARCANE USING COLD TECHNOLOGY AND PRODUCTS CONTAINING THE SAME

Systems, apparatuses, and methods for producing and using a sugarcane syrup or powder. In one embodiment, the invention is directed to a system and associated processes for processing sugarcane using a cold processing pipeline in a manner that retains its natural nutritional value while producing a syrup or powder without significant separation of the natural nutrients or use of heat or synthetic chemicals. 1. A method for processing raw sugarcane , comprising:soaking the raw sugarcane in a first bio-acidifier solution;juicing the soaked raw sugarcane to produce raw sugarcane juice;conditioning the raw sugarcane juice by adding a second bio-acidifier solution;reducing the temperature of the conditioned raw sugarcane juice by passing the conditioned raw sugarcane juice through a cooling component;subjecting the cooled raw sugarcane juice to an evaporation step to produce a syrup, wherein the evaporation step temperature is maintained below 40° C. until the brix value reaches a maximum of 68 to avoid crystallization of the syrup; andsubjecting the produced syrup to a process performed at a temperature between 2 and 4° C. to prevent degradation from microbiological activity, prior to packaging.2. The method of claim 1 , wherein the first and second bio-acidifier solutions consist of lime juice claim 1 , lemon juice claim 1 , citric acid claim 1 , or ascorbic acid.3. The method of claim 1 , wherein the raw sugarcane is soaked in the first bio-acidifier solution for a period of between 2 to 4 hours claim 1 , and the first bio-acidifier solution comprises a concentration of between 0.01-0.5% by weight of the lime juice claim 1 , lemon juice claim 1 , citric acid claim 1 , or ascorbic acid.4. The method of claim 1 , wherein the juicing of the soaked raw sugarcane is performed using a roller mill.5. The method of claim 1 , wherein the raw sugarcane juice is conditioned by adding the second bio-acidifier solution until the pH reaches a value between 3.5 and 4.2.6. The method ...

METHOD OF INCREASING WATER SOLUBLE NUTRIENT EXTRACTION FROM PLANT MATTER

Improved processes for extracting water soluble nutrients including sugars from plants and in particular sugar cane. The plants may be washed with a wash solution. After washing, water soluble nutrient containing liquid is extracted from the plants. A diluted wash solution may be added to the crushed plants to improve the extraction of the water soluble nutrients. The wash solution may be added to the liquid collected during the extraction to improve the separation of impurities from the nutrient containing liquid. The extracted liquid may demonstrate at least one of improved purity, improved clarity, improved filtration times, improved whiteness, and improved total recovered water soluble nutrients. 1. A process for extracting one or more water soluble nutrients from a plant material , comprising:washing the plant material with a wash solution comprising a surface activating agent and a hydroxide solution; andextracting the one or more water soluble nutrients from the plant material.2. The process of claim 1 , wherein the surface activating agent is selected from the group consisting of an anionic surfactant claim 1 , a non-ionic surfactant claim 1 , or combinations thereof.3. The process of claim 1 , wherein the surface activating agent includes at least one of a fatty acid claim 1 , a salt of a fatty acid claim 1 , or combinations thereof.4. The process of claim 1 , wherein the surface activating agent includes oleic acid claim 1 , a salt of oleic acid claim 1 , or combinations thereof.5. The process of claim 1 , further comprising a compatibilizing agent claim 1 , wherein the compatibilizing agent is an alcohol.6. The process of claim 5 , wherein the alcohol is selected from the group consisting of ethanol claim 5 , glycerin claim 5 , or combinations thereof.7. The process of claim 5 , wherein the surface activating agent is in a range of from 20% to 40% claim 5 , the compatibilizing agent is in a range of from 30% to 50% claim 5 , and the hydroxide solution in ...

DIARYL CARBONATE AND METHOD FOR PRODUCING THE SAME, AND METHOD FOR PRODUCING AN AROMATIC POLYCARBONATE RESIN

A diaryl carbonate containing a compound of the following formula (I) in an amount of less than 1,000 ppm by mass, and a method for producing the same: 2. A method for producing the diaryl carbonate according to claim 1 , the method comprising:a first step of reacting urea with an alkyl alcohol to yield a first reaction mixture containing a dialkyl carbonate;a second step of reacting the dialkyl carbonate in the first reaction mixture with an aryl alcohol to yield a second reaction mixture containing an alkylaryl carbonate;a third step of subjecting the alkylaryl carbonate in the second reaction mixture to disproportionation to yield a third reaction mixture containing a diaryl carbonate; anda fourth step of purifying the third reaction mixture,wherein the third reaction mixture further contains the compound of the formula (I) in an amount of 1,000 ppm by mass or more.3. The method according to claim 2 , wherein the fourth step comprises a distillation step of claim 2 , using a distillation column claim 2 , obtaining the diaryl carbonate containing the compound of the formula (I) in an amount of less than 1 claim 2 ,000 ppm by mass from the top of the column and obtaining a mixture having concentrated the compound of the formula (I) from the bottom of the column claim 2 , wherein the distillation step is conducted under the following conditions (a) and (b):(a) that the pressure at the top of the distillation column is 0.01 to 10 kPa, and(b) that the reflux ratio is 2 to 20.4. The method according to claim 3 , which further comprises a fifth step of filtering off the compound of the formula (I) which is precipitated from the concentrated mixture at a temperature in the range of from 80 to 230° C.5. The method according to claim 4 , which further comprises a recycling step (sixth step) of recovering the compound of the chemical formula (I) filtered off in the fifth step and bringing the filtrate back to the fourth step.6. The method according to claim 2 , wherein the ...

DISTRIBUTOR FOR A SCROLL SCREEN CENTRIFUGAL SEPARATOR

A scroll screen centrifugal separator includes a distributor that is configured to receive slurry received from a feed conduit. The distributor is configured to deflect the received slurry to a screen of the scroll screen centrifugal separator. In some embodiments, the distributor may include a distributor that has a flat surface encircled by a lip or having one or more lips positioned on the flat surface, an inclined surface, or a declined surface that faces the mouth of the feed conduit. In other embodiments, the distributor may include a plurality of dam members for defining passageways through which slurry is passable through the distributor prior to being ejected to a screen of the separator. In other embodiments, the distributor may include a distributor plate that has a plurality of radial arms attached thereto that are configured to direct slurry to the basket with a rotational velocity. 1. A distributor for a scroll screen centrifugal separator comprising:a first plate having a substantially flat surface for facing toward a mouth of a feed conduit when the first plate is attached within a scroll screen centrifugal separator, the substantially flat surface being inclined or declined such that a peripheral portion of the first plate is thicker than an inner portion of the first plate.2. A distributor for a scroll screen centrifugal separator comprising:a first plate having a surface and an opening for receiving slurry; andat least one lip attached to the first plate, each lip extending from the surface toward a mouth of a feed conduit such that an outermost portion of the lip is located closer to the mouth of the feed conduit as compared to the surface of the first plate when the distributor is mounted in a scroll screen centrifugal separator.3. The distributor of wherein the outermost portion of each lip defines an outermost surface of the lip claim 2 , the outermost surface of the lip being inclined claim 2 , declined claim 2 , staged claim 2 , stepped ...

METHOD FOR CONTROLLING THE OPERATION OF A CONTINUOUSLY OR PERIODICALLY OPERATING CENTRIFUGE AND DEVICE FOR CONDUCTING THE METHOD

A method for controlling the operation of a continuously or periodically operating centrifuge can be employed in the sugar industry for separating crystalline carbohydrates or sugar alcohols from a crystal suspension called a magma or a mother liquor. The magma has a varying content of fine grain that is dependent on the properties of the pretreatment and of the raw material. Variable control values are provided in a control device of the centrifuge. One or plurality of sensors are provided that carry out the measurements in electromagnetic, optical, acoustic, and/or conductive ways. These measurements that are conducted serve for determining the fine grain fraction of the magma. The measurements are supplied as measurement signals to the control device of the centrifuge. The control device automatically analyzes the measurement signals supplied to it and evaluates them with respect to the fine grain content of the magma. The control device changes the variable control values of the centrifuge as a function of this evaluation. 1. A method for controlling the operation of a continuously or periodically operating centrifuge ,which can be employed in the sugar industry for separating crystalline carbohydrates or sugar alcohols from a crystal suspension called a magma or a mother liquor,wherein the magma has a varying content of fine grain that is dependent on the properties of the pretreatment and of the raw material,with variable control values in a control device of the centrifuge,is hereby characterizedin that one or a plurality of sensors are provided that carry out the measurements in electromagnetic, optical, acoustic, and/or conductive ways,in that these measurements that are conducted serve for determining the fine grain fraction of the magma,in that the measurements are supplied as measurement signals to the control device of the centrifuge,in that the control device automatically analyzes the measurement signals supplied to it and evaluates them with respect ...

CONTAINER SET AND SAMPLE PREPARATION METHOD USING SAME

A container set including: a filter unit; and a closing unit that is attachable to and detachable from the filter unit. The filter unit includes: a housing having a sample introduction opening provided at one end, and a liquid discharging opening provided at the second end; and a filter fixed to the housing. The housing has a first joining part, and the closing unit has a second joining part configured to be joinable with the first joining part. The first joining part and the second joining part are configured such that the liquid discharging opening is spatially closed in a state in which the two joining parts are joined together. A space between the closing unit and the filter is made into a positive pressure relative to a pressure in the sample holding space by pushing the filter unit and the closing unit such that the distance therebetween is shortened. 1. A container set comprising:a filter unit; anda closing unit that is attachable to and detachable from the filter unit, wherein a housing having a first end including a closable sample introducing opening formed therein and a second end including a liquid discharging opening formed therein; and', 'a filter fixed to the housing,, 'the filter unit includesthe sample introducing opening is configured to allow solids and liquids to be therethrough introduced into a sample holding space surrounded by the housing and the filter,the liquid discharging opening is configured to allow a filtrate transmitted through the filter to be therethrough discharged,the housing of the filter unit has a first joining portion,the closing unit has a second joining portion that is joinable to the first joining portion,the first joining portion of the filter unit and the second joining portion of the closing unit are configured such that the first and second joining portions are joinable to each other to produce an airtight state to close the liquid discharging opening spatially by the closing unit, and such that the filter unit and the ...

COVER FOR CENTRIFUGAL FILTER

The present invention relates to a cover for a centrifugal filter, and is intended to propose a cover for a centrifugal filter, in which when water separated from oil is discharged through outlets provided in covers, the cover for the centrifugal filter can reduce the amount of oil leaking out with mixed gas and water. According to the present invention, there is provided a cover for a centrifugal filter, the cover constituting the centrifugal filter by covering a rotor that rotates so as to filter impurities contained in oil by using a centrifugal force, the rotor being provided with at least one nozzle through which filtered oil is jetted, the cover including: an inner cover configured to cover the rotor, the inner cover including a first outlet and a first inlet; an outer cover provided outside the inner cover; and an oil leak prevention member provided in the first outlet. 12021. A cover for a centrifugal filter , the cover constituting the centrifugal filter by covering a rotor () that rotates so as to filter impurities contained in oil by using a centrifugal force , the rotor being provided with at least one nozzle () through which filtered oil is jetted , the cover comprising:{'b': 110', '20', '111', '21', '112, 'an inner cover () configured to cover the rotor (), the inner cover including a first outlet () for discharging water separated from oil jetted from the nozzle (), and a first inlet () through which mixed gas is introduced into the inner cover;'}{'b': 120', '110', '1', '111', '2', '112', '110', '121', '1', '122', '2, 'an outer cover () provided outside the inner cover () such that an outlet chamber (C) communicating with the first outlet () and an inlet chamber (C) communicating with the first inlet () are provided outside the inner cover (), the outer cover being provided with a second outlet () communicating with the outlet chamber (C), and a second inlet () communicating with the inlet chamber (C); and'}{'b': 130', '111', '110', '110, 'an oil leak ...

COLLECTION, FILTRATION AND CONCENTRATION APPARATUS FOR BIOLOGICAL SAMPLES

The present disclosure describes a closed apparatus for collection, filtration and concentration of biological samples, such as fecal material. The sample is collected with an integrated sample collection device which introduces the sample into a transport liquid in a sample collection tube which couples to a filter unit coupled to a processing tube containing a processing liquid. The apparatus may be introduced into a centrifuge for centrifugal filtration. 1. A sample collection , filtration and processing apparatus , comprising:a sample collection tube containing a transportation liquid and having a first open end and a second open end opposite the first open end, the sample collection tube first open end configured to couple to a first removable cap, the first removable cap including an integrated sample collection device;a matched sample processing tube containing a processing liquid and having a sample processing tube first open end and a sample processing tube second closed end opposite the processing tube first open end; anda matched filter unit having a first open end and a second open end opposite the filter unit first open end, the filter unit first open end configured to couple to the sample collection tube open end, and the filter unit second open end configured to couple to the sample processing tube open end.2. The sample collection claim 1 , filtration and processing apparatus of claim 1 , wherein the integrated sample collection device comprises a shank with a scoop.3. The sample collection claim 1 , filtration and processing apparatus of claim 1 , further comprising a second removable cap configured to couple with and close the sample collection tube second open end.4. The sample collection claim 3 , filtration and processing apparatus of claim 3 , wherein the second removable cap has a flared fitting.5. The sample collection claim 1 , filtration and processing apparatus of claim 1 , wherein the filter unit first open end is configured to couple to ...

NOVEL SUCROSE UNASSIMILATING FLOCCULENT YEAST

An object of the present invention is to provide a sucrose unassimilating yeast which has a flocculation ability and has much of a proven performance of food production. The present invention pertains to a yeast strain expressed by accession number: NITE BP-1587. 1Saccharomyces cerevisiae. strain NITE BP-1588.2Saccharomyces cerevisiae. The strain according to claim 1 , wherein the strain is employed for a method of producing sugar and ethanol comprising a step of fermenting sugar liquid derived from a plant with yeast.3Saccharomyces cerevisiae. The strain according to claim 1 , wherein the strain is employed for a method of producing sugar and ethanol comprising steps of:removing non-sugar components contained in sugar liquid derived from a plant to clarify the sugar liquid; andadding yeast to the clarified sugar liquid to carry out ethanol fermentation at a given temperature under an anaerobic condition for an appropriate length of time.4Saccharomyces cerevisiae. A method of producing sugar and ethanol comprising a step of fermenting sugar liquid derived from a plant with the strain according to .5. A method of producing sugar and ethanol comprising steps of: removing non-sugar components contained in sugar liquid derived from a plant to clarify the sugar liquid; and{'i': 'Saccharomyces cerevisiae', 'claim-ref': {'@idref': 'CLM-00001', 'claim 1'}, 'adding the strain according to to the clarified sugar liquid to carry out ethanol fermentation at a given temperature under an anaerobic condition for an appropriate length of time.'}6Saccharomyces cerevisiae. strain NITE BP-1587 obtained by a breeding method comprising:subjecting a yeast strain deposited under accession number NBRC 10055 and a yeast strain deposited accession number NITE BP-1589 to spore isolation to acquire an isolated spore showing type a or type a as a mating type;mating the isolated spore of the yeast strain deposited under accession number NBRC 10055 and the isolated spore of yeast strain deposited ...

Horizontal centrifugal slurry filter removes filtrate and cake - in sequence controlled by internal vibration-responsive sensors

Slurry from a valved feeder enters one end face of a centrifuge filter rotating aobut a horizontal shaft, and builds up a bed of solids against the peripheral drum wall, detained by a filter fabric on a support mesh thorugh which filtrate travels to an integral colletor channel at the opposite end face. Collected filtrate is taken from the channel, to a container providing recovering liq. by a cranked pipe pivoted into suctional engagement with the channel contents. A sensor, pref. of source type, above the forming cake indicates that the supernatant liq. has reached its more-desirable height. Withdrawal of filtrate stops to be followed by extn. of the cake until the filter fabric is again exposed, whereupon the cycle re-commences. The sensors respond to vibratory changes in the pipes removing filtrate or cake. ADVANTAGE - Gases cannot enter below the filtration layers.

Kontinuerlig centrifugaltork

一种配药器

本发明涉及一种配药器，一种配药器，包括连接座和吸引件，所述连接座内设置有进液腔和输液腔，吸引件设置于所述连接座一端，所述吸引件包括气室，气室与进液腔、输液腔相连通，气室与进液腔之间设置有单向阀一，单向阀一的流向是从进液腔流向气室，气室与输液腔之间设置有单向阀二，单向阀二的流向是从气室流向输液腔，连接座相对气室的另一端设置有穿刺针，穿刺针包括第一通道，第一通道与进液腔相连通，连接座对应输液腔的一侧设置有与输液腔相连通的输液部。通过采用上述技术方案，操作简单，方便，零件少，结构简单，方便组装，生产成本低，输液部可与输液管连接，也可与穿刺针连接，可根据需求进行更换，方便配药操作，实用性更强。

Schlaufenreaktor

Centrifuge for separating solid particles from liquid

1449926 Centrifugal separators DONALDSON CO INC 15 Feb 1974 [28 Feb 1973] 7023/74 Heading B2P A centrifuge for separating particulate matter from a fluid comprises a stationary enclosure 12, Figs. 1 and 2, having fluid inlet means 44 and outlet means 16, a rotor 23 mounted within the enclosure for rotation about a predetermined axis, the rotor being constructed to receive uncleaned fluid from the inlet means and to deliver cleaned fluid to the outlet means and defining about the rotational axis a plurality of concentric passages for the fluid, and means associated with the rotor for causing fluid flowing therethrough to attain maximum angular momentum after leaving the plurality of passages. The rotor 23 is secured by screws 25 to a support plate 22 on the end of a rotatable shaft 19. The upper edge portion of the side wall 26 of the rotor is provided with threaded bores which receive Allen screws 27 having liquid flow restrictive bores 28. An annular top plate 29 is removably secured to the side wall 26. An annular baffle plate 32 is spacedly suspended from the plate 29 and defines with the side wall 26 a flow restrictive annular passage 35 disposed at the maximum radial point within the rotor 23. An annular member 36 of L-shaped cross-section is supported on the underside of baffle plate 32. The rotor also comprises a removable cartridge 37 defined by a liner tray having inner and outer cylindrical walls 38a, 38b and a bottom 38c. Disposed within the tray above spacers 38d are four particle separation stages or cartridge elements 39a-d each consisting of a flat layer 41, Fig. 5, of liquid impervious material, e.g. treated heavy paper or flexible cardboard, which is alternately wrapped with a corrugated layer 42 of the same materials, the size of the corrugations determining the spacing between the layers 41 and hence the depth of liquid flow therethrough. The separation stages 39a-d have progressively smaller spacing between the layers 41 to accommodate particles ...

稀释液制造装置及稀释液制造方法

稀释液制备装置(10)具有：第一配管(11)，其供给第一液体；第二罐(12a)，其贮存第二液体；第二配管(13)，其连接第一罐(12a)与第一配管(11)；压力调整部(18)，其调整第一罐(12a)内的压力，并将第一罐(12a)内的第二液体经由第二配管13进行加压输送而供给至第一配管(11)；控制部，其根据在第一配管(11)内流动的第一液体或稀释液的流量和稀释液的浓度的测量值，来调整基于压力调整部(18)的第二液体向第一液体的添加量，使得稀释液的浓度成为给定的浓度；以及第二罐(12b)，其与第一罐(12a)串联连接，临时储存向第一罐(12a)补充的第二液体。

Fan module which can separate dust and dust separating device for the same

PURPOSE: A fan module and a dust collector for the module are provided to effectively remove dust contained in air inhaled to the inside of a case of an electronic device using the centrifugal force. CONSTITUTION: A fan module(100) comprises the following: a dust collector(120) including a rotating space, an inhaling hole, and an exhaling hole; and a fan(110) flowing air to the inside of the rotating space while being connected with one side of the dust collector. The dust collector includes the following: a housing(131) with a rotation space in the inside, and an inlet connected to the rotation space; a rotation inducing member inducing the air to spirally rotate; a guiding partition(141) surrounding the exhaling hole; and a dust collecting box(150) collecting dust at the rotating space.

一种采用机械搅拌和罐外自动清洗锤度仪探头的卧式连续结晶罐

本发明公开了一种新型的采用机械搅拌和罐外自动清洗锤度仪探头的卧式连续结晶罐及在卧式连续结晶罐中采用机械搅拌实现强制循环和自动清洗锤度仪探头的方法，其特征在于：卧式连续结晶罐罐体内中部设一块横向隔板将长槽形罐体分隔成二个独立封闭的分室，在每个分室中央均设置有一个垂直列管式加热体，每个分室又被横向隔板和纵向隔板分隔成2～4个上部连通的隔室，在每个隔室的加热体和结晶罐罐壁之间形成一条降液通道，在降液通道中部设置有一套可在罐外自动清冼的锤度仪探头装置，在每个隔室的降液通道下部或加热体底部均装有1～2台机械搅拌器，能保证连续结晶罐在整个煮炼过程中始终保持良好的对流循环和把探头真正清洗干净。

Filtering centrifuge with attrition zone, mainly for extraction of starch from potato raw material

FIELD: food industry. SUBSTANCE: invention relates to starch production and is intended, mainly, for extraction of starch suspension from potatoes and can also be used for separation of raw materials of vegetable origin. Filtering centrifuge with an attrition unit, mainly for extraction of starch from potato raw material, comprises a stationary body with devices of material feed and discharge of separated phases, a drive and a rotary driven fitted on a shaft rotor with a filtering conical screen fixed on a disc with grinding elements of the attrition unit. Herewith the attrition unit is equipped on the feed device side with the disc with grinding elements, which shaft with own rotation speed from the drive is installed in the shaft of the disc with the screen, and between opposed grinding elements of the discs there is a narrowing to the screen slot, and the disc located on the side of the feed device also has on its side grinding elements, between which there are holes in the disc for channels to inlet the attrited material into the slot. EFFECT: technical result is higher efficiency of destruction of potato raw material cell structures and increased intensity of starch extraction from the potato raw material. 1 cl, 4 dwg РОССИЙСКАЯ ФЕДЕРАЦИЯ (19) RU (11) (13) 2 599 667 C1 (51) МПК B04B 5/10 (2006.01) B04B 3/00 (2006.01) B02C 7/00 (2006.01) C08B 30/02 (2006.01) ФЕДЕРАЛЬНАЯ СЛУЖБА ПО ИНТЕЛЛЕКТУАЛЬНОЙ СОБСТВЕННОСТИ (12) ОПИСАНИЕ (21)(22) Заявка: ИЗОБРЕТЕНИЯ К ПАТЕНТУ 2015123780/05, 19.06.2015 (24) Дата начала отсчета срока действия патента: 19.06.2015 (45) Опубликовано: 10.10.2016 Бюл. № 28 2 5 9 9 6 6 7 R U (54) ФИЛЬТРУЮЩАЯ ЦЕНТРИФУГА С ЗОНОЙ ИСТИРАНИЯ, ПРЕИМУЩЕСТВЕННО ДЛЯ ВЫДЕЛЕНИЯ КРАХМАЛА ИЗ КАРТОФЕЛЬНОГО СЫРЬЯ (57) Реферат: Изобретение относится к крахмалопаточному измельчающими элементами, вал которого с производству и предназначено, преимущественно, собственной скоростью вращения от привода для выделения крахмальной суспензии из установлен в вале диска с ситом ...

Способ центробежного разделения утфеля первой кристаллизации сахарного производства

Изобретение относится к сахарной промышленности. Способ разделения утфеля первой кристаллизации, предусматривающий загрузку утфеля в ротор фильтрующей центрифуги периодического действия, отделение первого оттека от кристаллов сахара, промывание их с отделением второго оттека и подсушивание кристаллов сахара перед выгрузкой из ротора. Предварительно в утфель, загружаемый в ротор, вводят моноглицерид дистиллированный мягкий, нагретый до температуры утфеля, в количестве 0,002-0,006% к его массе. Затем их смесь раскачивают сиропом концентрацией 60-65% с доведением содержания сухих веществ утфеля до 91,7-92,5%. После чего заполняют им ротор центрифуги одновременно с вводом в него воздуха, насыщенного влагой, температурой выше, чем у утфеля, на 5-7°C. Причем после отделения из слоя утфеля основной массы первого оттека, начинают промывание кристаллов сахара. Его осуществляют в две ступени - сначала сахарсодержащим раствором, затем горячей водой, смешанной с озоном. Изобретение обеспечивает увеличение выхода кристаллического белого сахара из центрифуги и улучшение его качественных показателей. 1 пр. РОССИЙСКАЯ ФЕДЕРАЦИЯ (19) RU (11) (13) 2 619 282 C2 (51) МПК C13B 30/10 (2011.01) ФЕДЕРАЛЬНАЯ СЛУЖБА ПО ИНТЕЛЛЕКТУАЛЬНОЙ СОБСТВЕННОСТИ (12) ФОРМУЛА (21)(22) Заявка: ИЗОБРЕТЕНИЯ К ПАТЕНТУ РОССИЙСКОЙ ФЕДЕРАЦИИ 2015144695, 19.10.2015 (24) Дата начала отсчета срока действия патента: 19.10.2015 Дата регистрации: Приоритет(ы): (22) Дата подачи заявки: 19.10.2015 (43) Дата публикации заявки: 03.05.2017 Бюл. № 13 Адрес для переписки: 109004, Москва, ул. Земляной вал, 73, ФГБОУ ВО "МГУТУ им. К.Г. Разумовского (ПКУ)", начальнику патентного бюро Самосват Д.А. (56) Список документов, цитированных в отчете о поиске: RU 2508408 A, 27.02.2014. SU 612961 A1, 30.06.1978. SU 1576570 A1, 07.07.1990. RU 2150507 С1, 10.06.2000. 2 6 1 9 2 8 2 R U (57) Формула изобретения Способ разделения утфеля первой кристаллизации, предусматривающий загрузку утфеля в ротор фильтрующей центрифуги периодического ...

Method of automatic control over process of dissolving salts

Изобретение относится к технике управления процессом растворения применительно к растворению карналлитовых руд с получением обогащенного карналлита. Способ включает стабилизацию температуры растворения солей и концентрации полезного компонента в растворе изменением расхода сырья на растворение, определение полезного компонента с входящими в процесс солями и корректировку расхода полезного компонента, поступающего в составе сырья. Определение полезного компонента в сырье - карналлитовой руде, горячем осветленном насыщенном растворе, обогащенном карналлите и охлажденном на вакуум-кристаллизационной установке (ВКУ) растворе после выделения из него обогащенного карналлита осуществляют по содержанию в потоках хлористого калия, стабилизацию концентрации полезного компонента ведут по осветленному насыщенному раствору, являющемуся выходным потоком процесса растворения, с корректировкой расхода полезного компонента, поступающего в составе сырья, с учетом расходов и составов обогащенного карналлита и охлажденного раствора с подачей вычисленных значений в качестве задания в систему управления расходом руды. Технический результат: упрощение процесса за счет стабилизации содержания полезного компонента, определяемого по хлористому калию, с корректировкой расхода руды по выходному потоку - осветленному раствору. 1 з.п. ф-лы, 2 табл., 2 пр. РОССИЙСКАЯ ФЕДЕРАЦИЯ (19) RU (11) (13) 2 598 937 C2 (51) МПК C01D 3/08 (2006.01) G05D 27/00 (2006.01) B01F 1/00 (2006.01) ФЕДЕРАЛЬНАЯ СЛУЖБА ПО ИНТЕЛЛЕКТУАЛЬНОЙ СОБСТВЕННОСТИ (12) ОПИСАНИЕ (21)(22) Заявка: ИЗОБРЕТЕНИЯ К ПАТЕНТУ 2015101827/05, 21.01.2015 (24) Дата начала отсчета срока действия патента: 21.01.2015 (43) Дата публикации заявки: 10.08.2016 Бюл. № 22 (73) Патентообладатель(и): Акционерное общество "ВНИИ Галургии" (АО "ВНИИ Галургии") (RU) R U Приоритет(ы): (22) Дата подачи заявки: 21.01.2015 (72) Автор(ы): Сафрыгин Юрий Степанович (RU), Осипова Галина Владимировна (RU), Тимофеев Владимир Иванович (RU), Панасюк Евгений Борисович (RU) ...

Apparatus for mixing solid and liquid substances

The method of mixing solid and liquid substances comprises the steps of keeping the substances in a constant circulation through a mixing tank by pumping the substances through a tank outlet and feeding them back through a tank inlet, discharging ready mixture from the tank, and supplying simultaneously a quantity of substances to the tank that equals the quantity of the ready mixture discharged from the tank. The apparatus for performing the method comprises a loop-type reactor with a reactor housing having inlet means at one end and outlet means at the opposite end, and having a tube socket for introducing the substances into the reactor. A control valve regulates the quantity of substances admitted to the reactor. The inlet means and the outlet means are interconnected by a pipe line, including a circulating pump. The pump keeps the substances in a constant flow through the reactor and the pipe line. A discharge valve is connected to the pipe line for discharging part of the ready mixture. A suitable connection between the discharge valve and the control valve causes the latter to feed such a quantity of substances to the reactor that equals the quantity of the ready mixture withdrawn through the discharge valve.

A kind of brown sugar boiling method

本发明属于糖加工领域，主要涉及一种制糖工艺，依次包括以下步骤：1)糖汁的提取；2)对糖汁进行絮凝沉淀；3)对絮凝沉淀好的糖汁进行膜机过滤；4)利用离子交换树脂进行进一步吸附除杂；5)蒸发浓缩；6)结晶过滤；7)喷干。采用本发明的所述的技术方案，具有如下的优点：1)和传统的制糖工艺相比，本发明使用高分子有机无机复合絮凝剂，絮凝沉淀不需要加热，可以避免加热对色值的影响，吸附强，过滤容易；2)同时采取离子交换树脂与膜过滤对糖汁进行深加工，可以制备获得优质的糖；3)工艺简单，效率高。

Automatic solvent aspirated powder feeder-dissolver

A method for dissolving chemical powders in water to make lumpfree solutions is afforded by this invention. The invention provides a method and an apparatus whereby water solutions of chemical powders can be easily formed. The method used to accomplish these results consists of the following: 1. Supplying a quantity of water to water supply port. 2. Feeding chemical powders through an outlet and into the water supply port, said water supply port having a supply assembly and a suction assembly fitted with aspirators to prevent backsplash and to draw the chemical powder into the water through the water supply port. 3. Mixing the chemical powders in the water in the water supply port to form a premixed slurry. 4. Discharging the premixed slurry into a mixing tank. 5. Filling a mixing tank and actuating a mixing means and a timer when the tank is filled to form a chemical solution. 6. Transferring the mixed solution to a storage tank by means of a transfer pump. 7. Pumping the chemical solution from the storage tank through a discharge. The apparatus used to accomplish the above method comprises: 1. A feeding chamber having an outlet. 2. A water supply port, comprising: A. a suction assembly having ends, B. a supply assembly having ends, C. two aspirators adapted to fit said ends of said suction assembly and the supply assembly, D. an automatic valve positioned in the supply assembly, and E. a delayed actuated automatic valve positioned between the suction assembly and the supply assembly. 3. A mixing tank capable of holding a chemical solution, comprising: A. a mixing means for the tank, B. an upper liquid-level-sensing means to close the automatic valve and the delayed actuated automatic valve, C. a lower liquid-level-sensing means to open said automatic valve and said delayed actuated automatic valve, D. an inlet adapted to receive said aspirator of said supply assembly of said water supply port, and E. an outlet. 4. A transfer pump adapted to remove said chemical ...

Apparatus for solving powder materials in liquid

Изобретение может быть использовано в химической и других област х промыншенности дл  растворени  порошкообразных материалов в жидкости . Оно обеспечивает повышение эксплуатационной надежности устройства и эффективности растворени  порошкообразных материалов. Устройство содержит камеры растворени  1 и 2 в виде обратньк конусов, трубопровод 3 подачи растворител  в эжектор 4. Камеры 1 и 2 в верхней части соединены тангенциальным патрубком 7. С эжектором 4 соединен сборник суспензии 8, установленный в ншйней части камеры растворени  2, Готовый раствор отводитс  из камеры, растворени  2 при помощи трубы 10 и попадает в емкость 11 дл  готового продукта, установленную на всасывающей линии-12 насоса 13. Устройство имеет загрузочное устройство 14. Наличие двух контуров циркул ции интенсифицирует процесс растворени  и снижает абразивный износ элементов конструкции, 1 ил. о The invention can be used in chemical and other industrial areas to dissolve powdered materials in a liquid. It provides an increase in the operational reliability of the device and the dissolution efficiency of powder materials. The device contains dissolution chambers 1 and 2 in the form of reverse cones, pipe 3 supplying solvent to the ejector 4. Chambers 1 and 2 in the upper part are connected by a tangential pipe 7. Suspension collector 8 connected to the ejector 4, installed in the inner part of the dissolution chamber 2, Ready solution discharged from the chamber, dissolving 2 by means of pipe 10 and entering the container 11 for the finished product installed on the suction line-12 of the pump 13. The device has a charging device 14. The presence of two circulation loops intensifies the process astvoreni and reduces abrasive wear of the structural elements 1 yl. about

Method of sugar production

FIELD: sugar industry. SUBSTANCE: invention relates to sugar industry. Method of sugar production, providing of boiling of the massecuite III crystallization, affinity of brown sugar III crystallization, extraction of the received affination fill-mass to separate the affinade from the affinity molasses. In this case, the brown sugar of III crystallization is affined with sugar syrup in a weight fraction of 38% to the mass of brown sugar at a temperature of 70°C for 20 minutes. Affinade is mixed with sugar syrup and briar powder and sugar is obtained with the addition of biologically-active agent, and the affinity molasses is given to the boiling point of the massecuite I crystallization. EFFECT: method allows to increase the output of finished sugar and reducing losses of sucrose in the crystallization process. 1 cl, 2 ex РОССИЙСКАЯ ФЕДЕРАЦИЯ (19) RU (11) (13) 2 647 507 C1 (51) МПК C13B 30/14 (2011.01) ФЕДЕРАЛЬНАЯ СЛУЖБА ПО ИНТЕЛЛЕКТУАЛЬНОЙ СОБСТВЕННОСТИ (12) ОПИСАНИЕ ИЗОБРЕТЕНИЯ К ПАТЕНТУ (52) СПК C13B 30/14 (2006.01) (21)(22) Заявка: 2016143510, 07.11.2016 (24) Дата начала отсчета срока действия патента: Дата регистрации: 16.03.2018 (45) Опубликовано: 16.03.2018 Бюл. № 8 2 6 4 7 5 0 7 R U (54) Способ производства сахара (57) Реферат: Изобретение относится к сахарной промышленности. Способ производства сахара, предусматривающий уваривание утфеля III кристаллизации, аффинацию желтого сахара III кристаллизации, центрифугирование полученного аффинационного утфеля для отделения сахарааффинада от аффинационного оттека. При этом желтый сахар III кристаллизации аффинируют сиропом сахарного производства массовой долей Стр.: 1 (56) Список документов, цитированных в отчете о поиске: Сапронов А.Р. и др. Технология сахара. Учебник. СПб.: ИД "Профессия", 2013. - с.159-160. RU 2150509 C1, 10.06.2000. RU 2340679 C1, 10.12.2008. RU 2266334 C2, 20.12.2005. UA 43704 A, 17.12.2001. RU 2054849 C2, 20.02.1996. 38% к массе желтого сахара при температуре 70°C в течение 20 минут. Сахар- ...

Vacuum centrifuge

FIELD: technological processes. SUBSTANCE: invention relates to centrifugal devices for separating suspensions containing components sensitive to mechanical influences as a solid phase. The centrifuge contains an outer casing, inside of which a perforated drum and an integrated turbomolecular pump are placed on the drive shaft. Rotor stages of turbomolecular pump are fixed on the drum shell near its loading opening, while the stator ones are made detachable and installed at least on two separate fragments of the outer casing shell. Fragments of the shell are made with the possibility of hermetic docking between themselves and the outer casing with the formation of a closed surface of rotation and equipped with drives of plane-parallel displacement relative to the axis of drum rotation. The contours of the radial sections of drum loading opening and the revolution surface, surrounding it with clearance, formed by the fragments of the outer casing shell are made along the profile of the Laval ring nozzle. In the receiving space of the centrifuge between the outer casing and the drum, in front of the rotor stages of turbomolecular pump, there are additionally installed drop eliminators fixed to the outer casing. EFFECT: preventing the filtrate removal through the turbine unit of the turbomolecular pump, increasing the degree of separation and drying of the suspension solid component due to inter-cavity air pressure drop. 4 dwg РОССИЙСКАЯ ФЕДЕРАЦИЯ (19) RU (11) (13) 2 631 951 C1 (51) МПК B04B 3/00 (2006.01) B04B 15/08 (2006.01) ФЕДЕРАЛЬНАЯ СЛУЖБА ПО ИНТЕЛЛЕКТУАЛЬНОЙ СОБСТВЕННОСТИ (12) ОПИСАНИЕ ИЗОБРЕТЕНИЯ К ПАТЕНТУ (21)(22) Заявка: 2017101647, 19.01.2017 (24) Дата начала отсчета срока действия патента: 19.01.2017 Дата регистрации: Приоритет(ы): (22) Дата подачи заявки: 19.01.2017 (45) Опубликовано: 29.09.2017 Бюл. № 28 (56) Список документов, цитированных в отчете о поиске: US 3822823 A, 09.07.1974. WO 2 6 3 1 9 5 1 R U (54) Вакуумная центрифуга (57) Реферат: ...

Open movable kettle for melting saccharine matter

Method of xylose extraction from solutions

FIELD: food industry. SUBSTANCE: invention relates to production of xylose used in confectionary industry and for preparing spices and xylitol. Method involves concentrating xylose an aqueous solution at xylose content 30-60 wt.-% to oversaturation state. Then solution containing 75-95 wt.-% of dry matter and with oversaturation degree index 1.1-3.0 is crystallized at cooling and stirring in the range of temperatures 80-20 C, preferably, at 65-25 C. Xylose crystals are extracted from crystalline mass. Biomass hydrolyzate, sulfide digesting solution of wood processing industry and other sources are used as the parent xylose solution. Method provides preparing xylose from solutions with its relatively low content with respect to dry matter of solution. EFFECT: increased efficiency of method as compared with known ones. 19 cl, 13 tbl ЗЕ0ДАГсС ПЧ с» (19) РОССИЙСКОЕ АГЕНТСТВО ПО ПАТЕНТАМ И ТОВАРНЫМ ЗНАКАМ ВИ ”” 2 177 038 (51) МПК” (13) С2 С1ЗК 13/00, СлЗЕ 1/02 (12) ОПИСАНИЕ ИЗОБРЕТЕНИЯ К ПАТЕНТУ РОССИЙСКОЙ ФЕДЕРАЦИИ (21), (22) Заявка: 97116164/13, 01.03.1996 (24) Дата начала действия патента: 01.03.1996 (30) Приоритет: 01.03.1995 Е 950957 (43) Дата публикации заявки: 20.07.1999 (46) Дата публикации: 20.12.2001 (56) Ссылки: 4$ 4168988 А, 25.09.1979. ОЕ 834079 А, 17.03.1952. Ц$ 5084104 А, 28.01.1992. СВ 2206293 А, 05.01.1989. $Ц 82023 А, 02.06.1949. Ц$ 4631129 А, 23.12.1986. ОЕ 1643940 А, 10.06.1970. (85) Дата перевода заявки РСТ на национальную фазу: 01.10.1997 (86) Заявка РСТ: Е! 96/00122 (01.03.1996) (87) Публикация РСТ: М/О 96/27028 (06.09.1996) (98) Адрес для переписки: 129010, Москва, ул. Большая Спасская 25, стр.3, ООО "Юридическая фирма Городисский и Партнеры", Лебедевой Н.Г. (71) Заявитель: . КСЮРОФИН ОИ (||) (72) Изобретатель: Мирья ЛИНДРООС ([|, Хейкки ХЕИККИЛЯ (;!), Юха НУРМИ (Е!), Олли-Пекка ЭРОМА ([) (73) Патентообладатель: КСЮРОФИН ОИ (>!) (74) Патентный поверенный: Лебедева Наталья Георгиевна (54) СПОСОБ ИЗВЛЕЧЕНИЯ КСИЛОЗЫ ИЗ РАСТВОРОВ (57) Изобретение ...

How to recover xylose from xylose solution

본 발명은 용해된 고체를 기준하여 크실로즈를 30 내지 60중량% 포함하는 크실로즈 함유 수용액을 처리하여 크실로즈로 과포화된 용액을 생성시키고 이로부터 크실로즈를 결정화시킨 다음, 크실로즈 결정을 회수함을 포함하는, 상기 크실로즈 수용액으로부터 크실로즈를 회수하는 방법에 관한 것이다. The present invention is to treat a xylose containing aqueous solution containing 30 to 60% by weight of xylose based on the dissolved solids to produce a solution supersaturated with xylose and crystallize the xylose therefrom and then recover the xylose crystals. It relates to a method for recovering xylose from the xylose aqueous solution comprising a.

Mixing ring for dissolving a portion of the soluble substance in a portion of the solvent, a system and a method of dissolving a portion of the soluble substance in a portion of the solvent

FIELD: mixing; machine building.SUBSTANCE: invention relates to a system, a method and to a mixing ring for dissolving a portion of a soluble substance in a portion of a solvent. Mixing ring for dissolving a portion of a soluble substance in a portion of the solvent contains: a solvent inlet path and a solute feed path, connected by fluid medium by mixing, wherein the solvent feed path is configured to receive a portion of the solvent, and the soluble substance feed path is configured to receive a portion of the solute, wherein the mixing ring is structurally configured to conduct a portion of the solvent and a portion of the soluble substance to the mixing path, and wherein the mixing ring further comprises a diffuser, mainly located in internal area of mixing path, wherein diffuser is configured to conduct portion of solvent to portion of soluble substance, wherein the soluble substance feed path comprises a projecting slope configured to direct a portion of the solute to the diffuser, wherein the protruding ramp sets the throat angle relative to the inner wall of the mixing ring, wherein the throat angle is an acute angle, wherein solvent feed path is made as solvent feed zone and throttling zone, wherein throttling zone is located between solvent feed zone and by mixing, wherein the connection between the solvent inlet zone and the throttling zone forms a first diameter, and the connection between the throttling zone and the mixing path forms a second diameter, which is smaller than first diameter, wherein inner diameter of throttling zone gradually decreases from first diameter to second diameter.EFFECT: technical result is reduction in consumption of dissolved substance.37 cl, 11 dwg РОССИЙСКАЯ ФЕДЕРАЦИЯ (19) RU (11) (13) 2 721 786 C2 (51) МПК B01F 5/06 (2006.01) B01F 3/12 (2006.01) B01F 5/04 (2006.01) ФЕДЕРАЛЬНАЯ СЛУЖБА ПО ИНТЕЛЛЕКТУАЛЬНОЙ СОБСТВЕННОСТИ (12) ОПИСАНИЕ ИЗОБРЕТЕНИЯ К ПАТЕНТУ (52) СПК B01F 5/06 (2020.02); B01F 3/12 (2020.02); B01F 5/04 (2020.02) ...

Water-soluble particle mixing and stirring mechanical equipment

本发明公开了一种水溶性颗粒混合搅拌机械设备，包括主体箱，所述主体箱下端左右两侧均设置有支撑腿，所述主体箱内底部右侧设置有过滤器，且过滤器下端设置有一号排料管，所述主体箱上端中部设置有一号电机，所述一号电机下端设置有搅拌轴，所述搅拌轴下端贯穿主体箱且连接主体箱内底部，所述搅拌轴中部设置有多个搅拌叶，且搅拌叶下端中部设置有副搅拌叶。本发明通过进料口、进料管、抽水泵和输水管的配合，使水溶性颗粒进行初步溶解并且增加水溶性颗粒的流动性，有利于进一步的溶解。本发明通过固定磨盘、转动磨盘、二号电机和齿轮的配合，将水溶性颗粒粉碎成细粉末，细粉末与水的接触面积更大，更加利于溶解。

Method for separating white sugar of i crystallization in a centrifugal force field

FIELD: sugar industry.SUBSTANCE: invention relates to the sugar industry. A method for separating the first crystallization massecuite, which involves feeding it into the centrifuge rotor, separating the massecuite, separating runoffs, washing sugar crystals, bringing them to a moisture content of 0.8-1.5% to their mass before unloading from the centrifuge rotor. The massecuite before being fed into the receiving massecuite mixer is pre-condensed in a vacuum apparatus to a content of 93.5-93.8% solids in it, then in the massecuite mixer the massecuite is pumped with the first outflow to 91.0-91.5% solids and before being fed into the centrifuge bring its temperature to 68-72°C. Separation of the massecuite in a force centrifugal field is carried out with a device for fixing the moment of separation of the intercrystalline solution from sugar crystals, which contains a housing and a sensitive element installed in it in the form of a plate, which is in contact with the flow of the separated intercrystalline solution and is connected to the centrifuge control unit.EFFECT: invention provides an increase in the yield of sugar from the centrifuge while reducing the water consumption for washing its crystals.1 cl, 1 ex РОССИЙСКАЯ ФЕДЕРАЦИЯ (19) RU (11) (13) 2 771 068 C1 (51) МПК C13B 30/10 (2011.01) ФЕДЕРАЛЬНАЯ СЛУЖБА ПО ИНТЕЛЛЕКТУАЛЬНОЙ СОБСТВЕННОСТИ (12) ОПИСАНИЕ ИЗОБРЕТЕНИЯ К ПАТЕНТУ (52) СПК C13B 30/10 (2021.08) (21)(22) Заявка: 2021114459, 21.05.2021 (24) Дата начала отсчета срока действия патента: Дата регистрации: 26.04.2022 (45) Опубликовано: 26.04.2022 Бюл. № 12 2 7 7 1 0 6 8 R U (56) Список документов, цитированных в отчете о поиске: RU 2251574 C1, 10.05.2005. SU 1578201 A1, 15.07.1990. SU 636034 A1, 05.12.1978. SU 1611936 A1, 07.12.1990. RU 1692043 C, 10.05.1995. GB 1127692 A, 18.09.1968. EP 3453772 A1, 13.03.2019. (54) СПОСОБ РАЗДЕЛЕНИЯ УТФЕЛЯ I КРИСТАЛЛИЗАЦИИ В СИЛОВОМ ЦЕНТРОБЕЖНОМ ПОЛЕ (57) Реферат: Изобретение относится к сахарной его температуру до 68-72°С. ...

CENTRIFUGE OF CYCLIC ACTION, IN PARTICULAR FOR SEPARATION OF MELASSES FROM SUGAR CRYSTALS IN UTFEL

1. Центрифуга циклического действия, в частности для отделения мелассы от кристаллов сахара в утфеле, содержащая барабан центрифугирования с проницаемой стенкой для загрузки в него обрабатываемых продуктов, привод вращения барабана вокруг вертикальной оси, разгрузочное устройство со средствами очистки внутренней поверхности проницаемой стенки барабана, выполненными в виде узла из по меньшей мере двух первой и второй лопат, расположенных внутри барабана и установленных с возможностью поворота вокруг вертикальной оси для перехода из отведенного положения, в котором лопата оказывает меньшее сопротивление вращению барабана, в контактное положение для очистки указанной проницаемой стенки барабана, причем лопаты выполнены с возможностью вертикального поступательного перемещения во время выгрузки продуктов, отличающаяся тем, что первая и вторая лопаты расположены со смещением по высоте барабана для очистки, соответственно, верхней и нижней частей барабана, при этом центрифуга дополнительно содержит средства вертикального поступательного перемещения второй лопаты с ограничением хода, средства вертикального поступательного перемещения первой лопаты с ограничением хода и средство независимого управления двумя лопатами. ! 2. Центрифуга по п.1, отличающаяся тем, что барабан (2) закреплен на валу (7) привода (3) на уровне ступицы (8), расположенной в нижней части барабана, при этом вторая лопата (6) выполнена с возможностью перемещения с ограничением хода в вертикальном направлении из промежуточного положения в барабане (2) для очистки нижней части барабана на уровне ступицы (8). ! 3. Центрифуга по любому из пп.1 или 2, РОССИЙСКАЯ ФЕДЕРАЦИЯ (19) RU (11) 2008 112 209 (13) A (51) МПК B04B 11/08 (2006.01) ФЕДЕРАЛЬНАЯ СЛУЖБА ПО ИНТЕЛЛЕКТУАЛЬНОЙ СОБСТВЕННОСТИ, ПАТЕНТАМ И ТОВАРНЫМ ЗНАКАМ (12) ЗАЯВКА НА ИЗОБРЕТЕНИЕ (21), (22) Заявка: 2008112209/12, 23.08.2006 (71) Заявитель(и): ФИВ КЭЛЬ (FR) (30) Конвенционный приоритет: 31.08.2005 FR 0508919 (85) Дата перевода заявки PCT на ...

SET AND DEVICE FOR SEATING NIVAN IN A CONTAINER CONTAINING FLUID MATERIAL

Method for obtaining the first fillmass

FIELD: sugar industry. SUBSTANCE: invention relates to the sugar industry. A method for obtaining the first fillmass, including thickening the syrup in a vacuum apparatus, winding the crystals, building them up, selecting a part of the fillmass, centrifuging this part of the fillmass with separation into sugar crystals and outflow, returning the outflow to the vacuum apparatus and boiling the remaining part of the fillmass until ready. As centers of crystallization, mother fillmass with crystal sizes of 0.120-0.160 mm is used, which are increased at a supersaturation coefficient of 0.12-0.15 and thickening of the fillmass to 88-90% of dry substances, this process is carried out to the content of 35-40% of crystals in the fillmass. The selection of a part of the fillmass is carried out for intermediate centrifugation in an amount of 30-45% of the total mass. The remaining fillmass in the vacuum apparatus is pumped with syrup mixed with the sugar of the second crystallization in equal quantities to the content of 88-90% of dry substances in the fillmass, distilled monoglyceride is added to it and the crystals are re-built on the syrup with a dry substance content of 65-70%. At the last pumping, the outflow obtained after intermediate centrifugation of the selected part of the fillmass is introduced into the vacuum apparatus and the process of thickening of the fillmass is carried out to 92.0-92.5% of dry substances. EFFECT: method provides an increase in the yield and quality of crystalline white sugar from the first fillmass. 1 cl РОССИЙСКАЯ ФЕДЕРАЦИЯ (19) RU (11) (13) 2 757 119 C1 (51) МПК C13B 30/02 (2011.01) ФЕДЕРАЛЬНАЯ СЛУЖБА ПО ИНТЕЛЛЕКТУАЛЬНОЙ СОБСТВЕННОСТИ (12) ОПИСАНИЕ ИЗОБРЕТЕНИЯ К ПАТЕНТУ (52) СПК C13B 30/02 (2021.08) (21)(22) Заявка: 2020141087, 14.12.2020 (24) Дата начала отсчета срока действия патента: Дата регистрации: 11.10.2021 (45) Опубликовано: 11.10.2021 Бюл. № 29 2 7 5 7 1 1 9 R U (56) Список документов, цитированных в отчете о поиске: RU 2227162 ...

A kind of Full automatic timing solution heating evaporation crystallizer chemical industry equipment

本发明公开了一种全自动定时溶液加热蒸发结晶器化工设备，包括机架，所述机架固定放置在地面上，所述机架内设有分层隔板，所述机架内第一层隔板设有溶液初步加热机构，所述溶液初步加热机构设有抽水机构，所述机架内第二层设有溶液蒸发结晶机构，所述溶液蒸发结晶机构设有蒸汽机构，所述溶液蒸发结晶机构设有冷凝水收集机构，所述机架内第三层隔板溶液过滤收集机构，所述溶液过滤收集机构设有废液处理机构，所述废液处理机构设有废液处理系统，所述控制器设有电容显示屏，所述控制器设有工业用电插口，所述控制器中设有PLC系统。本发明的有益效果是，结构简单，实用性强。

Method for separating white sugar of the first crystallization in a batch filter centrifuge

FIELD: sugar industry.SUBSTANCE: invention relates to the sugar industry. The method for separating the massecuite of the first crystallization, which involves loading the massecuite into centrifuges, separating the first outflow from the sugar crystals, feeding it to a sensitive element connected to the pneumatic power converter of the first outflow separation time control device, which is installed in the space between the casing and the centrifuge rotor, and on the inner surface of the casing, from where the first runoff flows down and is removed from the centrifuge using a segregator. Washing sugar crystals with separation of the second outflow and bringing the moisture content of sugar crystals to 0.8-1.5% by weight. Before feeding the massecuite into the rotor, it is kept in a massecuite mixer, swinging it with the first runoff, to which distilled monoglyceride is preliminarily added. Washing of sugar crystals starts when the pressure on the sensor of the first outflow reaches 0.09-0.10 MPa and is carried out in two stages sequentially, first with the first outflow, enriched earlier with distilled monoglyceride, and then with hot water.EFFECT: invention provides an increase in the output of sugar from the centrifuge.1 cl РОССИЙСКАЯ ФЕДЕРАЦИЯ (19) RU (11) (13) 2 771 067 C1 (51) МПК C13B 30/10 (2011.01) ФЕДЕРАЛЬНАЯ СЛУЖБА ПО ИНТЕЛЛЕКТУАЛЬНОЙ СОБСТВЕННОСТИ (12) ОПИСАНИЕ ИЗОБРЕТЕНИЯ К ПАТЕНТУ (52) СПК C13B 30/10 (2021.08) (21)(22) Заявка: 2021114460, 21.05.2021 (24) Дата начала отсчета срока действия патента: Дата регистрации: 26.04.2022 (45) Опубликовано: 26.04.2022 Бюл. № 12 2 7 7 1 0 6 7 R U (56) Список документов, цитированных в отчете о поиске: RU 2227810 C1, 27.04.2004. RU 2251574 C1, 10.05.2005. SU 636034 A1, 05.12.1978. RU 1692043 C, 10.05.1995. GB 1127692 A, 18.09.1968. EP 3453772 A1, 13.03.2019. (54) Способ разделения утфеля первой кристаллизации в фильтрующей центрифуге периодического действия (57) Реферат: Изобретение относится к сахарной влажности ...

Method for uniforming solution and solution tank

本发明公开了一种将溶液制备均匀的方法和溶液槽，所述方法主要是通过将溶液打在容器内液体折流装置上，使溶液折流打向容器底部，从而在容器内形成竖向旋窝，溶液互相碰撞、激荡、造成强烈紊流，实现快速混合；所述溶液槽主要由上部柱形壳体部分(100)和下部锥形壳体部分(200)组成，溶液槽内部设置有折流液体分布器(5)，折流液体分布器(5)由两个笠帽状装置(12、13)相扣组成，下笠帽装置(13)延边缘固定在上笠帽装置(12)扇面内侧，锥形壳体部分(200)下部设置有出液管(8)，出液管(8)内部设置有延伸至折流液体分布器(5)下方的与出液管(8)同心的循环进液管(7)。

Method for boiling out first crystallization fillmass in vacuum apparatus

FIELD: chemistry. SUBSTANCE: method for producing the first crystallization fillmass, comprising preparing the sugar melts of the second and third crystallization, the sugar melts condensation, the crystals formation by introducing crystallization centres, their extension and thickening the fillmass until ready. The formation of crystallization centres is carried out directly in the sugar melt of the second crystallization. The crystallization centres are represented by powdered sugar fractionated by sieve analysis to the crystals size of 0.120-0.160 mm at the rate of 5-6 pc. per 1 mm of the trial lens surface length. The crystallization centres extension is carried out in two stages, wherein at the second stage soft distilled monoglyceride is introduced. EFFECT: reducing the duration of boiling out the fillmass of the first crystallization, increasing the crystals percentage therein and reducing unaccounted losses of sugar. РОССИЙСКАЯ ФЕДЕРАЦИЯ (19) RU (11) (13) 2 619 308 C2 (51) МПК C13B 25/00 (2011.01) ФЕДЕРАЛЬНАЯ СЛУЖБА ПО ИНТЕЛЛЕКТУАЛЬНОЙ СОБСТВЕННОСТИ (12) ФОРМУЛА (21)(22) Заявка: ИЗОБРЕТЕНИЯ К ПАТЕНТУ РОССИЙСКОЙ ФЕДЕРАЦИИ 2015144696, 19.10.2015 (24) Дата начала отсчета срока действия патента: 19.10.2015 Дата регистрации: Приоритет(ы): (22) Дата подачи заявки: 19.10.2015 (43) Дата публикации заявки: 21.04.2017 Бюл. № 12 2 6 1 9 3 0 8 R U (56) Список документов, цитированных в отчете о поиске: RU 2371480 C1, 27.10.2009. RU 2133276 C1, 20.07.1999. RU 2479631 C1, 20.04.2013. SU 612961 A1, 30.06.1978. SU 1578201 A1, 15.07.1990. (54) СПОСОБ УВАРИВАНИЯ УТФЕЛЯ ПЕРВОЙ КРИСТАЛЛИЗАЦИИ В ВАКУУМ-АППАРАТЕ (57) Формула изобретения Способ получения утфеля первой кристаллизации, предусматривающий приготовление клеровок сахара второй и третьей кристаллизации, сгущение клеровок в вакуум-аппарате до состояния пересыщения (1,20-1,30), заводку кристаллов путем введения центров кристаллизации, их наращивание и сгущение утфеля до готовности перед спуском из аппарата в приемную ...

Method for producing layer-mineralized sugar

FIELD: food industry.SUBSTANCE: invention relates to sugar industry. Disclosed is a method of producing layer-mineralized sugar, comprising a set of a mixture of effluents of first and second fillmass II in vacuum apparatus of the last crystallisation step, condensation thereof, formation of crystallisation centers, growth of crystals until ready for descent. Crystals are grown such that 2/3 of the portion of the ready fillmass III is fed for cooling, followed by centrifugation, and on remaining in vacuum apparatus 1/3 part of fillmass III crystal growth is continued, pumping up the first effluent of fillmass II to ready fillmass for descent, after which 2/3 portions of the ready-to-run fillmass are directed into a receiving mixer and centrifuged, and on the remaining part of vacuum apparatus 1/3 of the fillmass part, crystal growth is continued, pumping out the first runoff of fillmass I until ready fillmass is ready for descent, then 2/3 of the part of the ready fillmass is delivered into a receiving stirrer and centrifuged, and on remaining part of vacuum apparatus 1/3 of the fillmass part one proceeds with growth of crystals till ready for descent by pumping out the obtained syrup from the evaporator plant. Then fillmass is lowered into receiving mixer and centrifuged with separation of two effluents to produce finished product.EFFECT: invention ensures production of sugar enriched with mineral substances.1 cl, 2 ex РОССИЙСКАЯ ФЕДЕРАЦИЯ (19) RU (11) (13) 2 687 591 C1 (51) МПК C13B 25/00 (2011.01) ФЕДЕРАЛЬНАЯ СЛУЖБА ПО ИНТЕЛЛЕКТУАЛЬНОЙ СОБСТВЕННОСТИ (12) ОПИСАНИЕ ИЗОБРЕТЕНИЯ К ПАТЕНТУ (52) СПК C13B 25/00 (2013.01) (21) (22) Заявка: 2018113162, 11.04.2018 (24) Дата начала отсчета срока действия патента: 11.04.2018 15.05.2019 (45) Опубликовано: 15.05.2019 Бюл. № 14 Адрес для переписки: 125080, Москва, Волоколамское ш., 11, ФГБОУ ВО "МГУПП" (73) Патентообладатель(и): Федеральное государственное бюджетное образовательное учреждение высшего образования "Московский ...

Pneumatic reaction liquid stirring device for chip packaging

本申请公开一种用于芯片封装的气动式反应液搅拌装置，包括筒体、设置在所述筒体内的喷嘴组件，所述喷嘴组件的前端形成有出气口；所述筒体的前端呈开放设置且超出所述出气口，所述筒体上还开设有进液口，所述进液口沿前后方向位于所述出气口的后方。本申请用于芯片封装的气动式反应液搅拌装置使用过程中，外部压缩气体自喷嘴组件的出气口吹出，利用所述出气口后方形成的负压吸引液体自进液口流入筒体，再随气流从筒体前方流出，进行高速循环流动，搅拌效果较好，利于溶质的溶解，很好地满足生产需求。

Method for automatic control of salt dissolution process

1. Способ автоматического управления процессом растворения солей, включающий стабилизацию температуры растворения солей и концентрации полезного компонента в растворе изменением расхода сырья на растворение, определение полезного компонента с входящими в процесс солями и корректировку расхода полезного компонента, поступающего в составе сырья, отличающийся тем, что определение полезного компонента в сырье - карналлитовой руде, горячем осветленном насыщенном растворе, обогащенном карналлите и охлажденном на вакуум-кристаллизационной установке (ВКУ) растворе после выделения из него обогащенного карналлита, осуществляют по содержанию в потоках хлористого калия, стабилизацию концентрации полезного компонента ведут по осветленному насыщенному раствору, являющемуся выходным потоком процесса растворения, с корректировкой расхода полезного компонента, поступающего в составе сырья, с учетом расходов и составов обогащенного карналлита и охлажденного раствора по следующим зависимостям с подачей вычисленных значений в качестве задания в систему управления расходом руды:,где C- содержание хлористого калия в карналлите, входящем в состав руды, %;C- общее содержание хлористого калия в руде, %;C- содержание свободного химически не связанного хлористого калия, входящего в состав руды, %;- содержание хлористого магния в руде, %:- содержание хлористого магния в жидкой фазе слива растворителей при условии насыщения раствора солями: MgCl, KCl, NaCl, %:t- температура осветленного раствора, °C;C- содержание хлористого калия в осветленном растворе, %;- содержание хлористого магния в осветленном растворе при степени его насыщения пои насыщенного хлористым РОССИЙСКАЯ ФЕДЕРАЦИЯ (19) RU (11) (51) МПК C01D 3/08 (13) 2015 101 827 A (2006.01) ФЕДЕРАЛЬНАЯ СЛУЖБА ПО ИНТЕЛЛЕКТУАЛЬНОЙ СОБСТВЕННОСТИ (12) ЗАЯВКА НА ИЗОБРЕТЕНИЕ (21)(22) Заявка: 2015101827, 21.01.2015 (71) Заявитель(и): Акционерное общество "ВНИИ Галургии" (АО "ВНИИ Галургии") (RU) Приоритет(ы): (22) Дата подачи заявки: 21.01.2015 (43) ...

Sugar beet juice purification method

A kind of brown sugar block refiningly cooks shaped device

本发明涉及红糖加工设备的技术领域，具体是一种红糖块炼煮成型装置，其包括红糖炼煮容器、成型输送带、风冷箱和成品输送带，成型输送带的一端上部安装有糖浆浇注机，成型输送带的另一端设置在风冷箱内，成型输送带的输送带上固定有红糖块成型模，红糖块成型模上设置有多个红糖块成型槽，成品输送带安装在成型输送带下部，成品输送带的另一端也设置在风冷箱内，成型输送带上安装有能将红糖块成型槽内的红糖块顶压脱落到成品输送带上的脱模顶压装置；红糖炼煮容器底部连接有输送管，红糖炼煮容器的底部与输送管的连接处设置有密封阀，输送管另一端连通至糖浆浇注机，输送管上安装有糖浆输送泵。本发明结构简单，设置巧妙，红糖块成型效率高。

Method and plant for evaporative concentration and crystallization of viscous lactose-containing aqueous liquid

FIELD: food-processing industry; separation of lactose from liquids obtained as byproducts of milk industry and allied branches. SUBSTANCE: proposed method consists in separation of crystalline mono-hydrate of α-lactose from viscous lactose-containing liquids by simultaneous heating, removal of evaporating steam and mechanical mixing. Plant proposed for realization of this method consists of three devices. One device has horizontal cylindrical housing, revolving horizontal shaft, blades extending radially from shaft towards cylindrical wall of housing and heating jacket. Plant is also provided with cooling unit and unit for grinding and drying. EFFECT: possibility of obtaining non-hygroscopic product possessing high looseness. 13 cl, 2 dwg, 1 ex ÐÎÑÑÈÉÑÊÀß ÔÅÄÅÐÀÖÈß (19) RU (11) 2 280 990 (13) C2 (51) ÌÏÊ A23C 1/12 A23C 1/00 (2006.01) (2006.01) ÔÅÄÅÐÀËÜÍÀß ÑËÓÆÁÀ ÏÎ ÈÍÒÅËËÅÊÒÓÀËÜÍÎÉ ÑÎÁÑÒÂÅÍÍÎÑÒÈ, ÏÀÒÅÍÒÀÌ È ÒÎÂÀÐÍÛÌ ÇÍÀÊÀÌ (12) ÎÏÈÑÀÍÈÅ ÈÇÎÁÐÅÒÅÍÈß Ê ÏÀÒÅÍÒÓ (21), (22) Çà âêà: 2004133562/13, 21.03.2003 (72) Àâòîð(û): ÕÅÍÍÈÍÃÔÈËÄ Òîìàñ Äýâèä (US), ÄÀÉÍÑÅÍ Ðè÷àðä Ýíäðþ (US) (24) Äàòà íà÷àëà îòñ÷åòà ñðîêà äåéñòâè ïàòåíòà: 21.03.2003 (73) Ïàòåíòîîáëàäàòåëü(è): ÍÈÐÎ À/Ñ (DK) R U (30) Êîíâåíöèîííûé ïðèîðèòåò: 17.04.2002 DK PA 2002 00567 (43) Äàòà ïóáëèêàöèè çà âêè: 20.04.2005 (45) Îïóáëèêîâàíî: 10.08.2006 Áþë. ¹ 22 2 2 8 0 9 9 0 (56) Ñïèñîê äîêóìåíòîâ, öèòèðîâàííûõ â îò÷åòå î ïîèñêå: US 5006204 À, 09.04.1991. US 5271163 À, 21.12.1993. US 6335045 B1, 01.01.2002. GB 740255 À, 09.11.1955. SU 827005, 07.05.1981. SU 1787411 À1, 15.03.1993. (85) Äàòà ïåðåâîäà çà âêè PCT íà íàöèîíàëüíóþ ôàçó: 17.11.2004 2 2 8 0 9 9 0 R U (87) Ïóáëèêàöè PCT: WO 03/086091 (23.10.2003) C 2 C 2 (86) Çà âêà PCT: DK 03/00193 (21.03.2003) Àäðåñ äë ïåðåïèñêè: 129010, Ìîñêâà, óë. Á.Ñïàññêà , 25, ñòð.3, ÎÎÎ "Þðèäè÷åñêà ôèðìà Ãîðîäèññêèé è Ïàðòíåðû", ïàò.ïîâ. Ñ.À.Äîðîôååâó (54) ÑÏÎÑÎÁ È ÓÑÒÀÍÎÂÊÀ ÄËß ÈÑÏÀÐÈÒÅËÜÍÎÃÎ ÊÎÍÖÅÍÒÐÈÐÎÂÀÍÈß È ÊÐÈÑÒÀËËÈÇÀÖÈÈ ÂßÇÊÎÉ ËÀÊÒÎÇÎÑÎÄÅÐÆÀÙÅÉ ÂÎÄÍÎÉ ÆÈÄÊÎÑÒÈ (57) Ðåôåðàò: ...

a method of treating oil wastewater in metalworking fluid

The present invention relates to a method for treating oil wastewater from a metalworking process using a continuous disk-type centrifuge in order to be reused as industrial water, through a process composed of a filtering pretreatment step, a precise filtering step, a hollow fiber membrane filtering step, a multimedia filter filtering step, and a reverse osmosis filtering step. The filtering pretreatment step can provide a simplified process, can remove oil and SS at the same time, can easily remove even emulsified oil with fine particles, can have a reduced facility installation area, can provide convenient operation and control of the facility, can save operation and maintenance costs by removing the need of additional cleaning work, and can provide continuous work. Because the filtering pretreatment step can reduce contamination loads by providing excellent efficiency in removing SS and oil substances, a filtering step using a separation membrane can perform continuous operation for a long time without any changes in a flow rate and can extend the life of the separation membrane during separation membrane filtering treatment.

Method of producing aqueous solution of slaked lime and apparatus therefor

내용 없음. No content.

SYSTEM AND METHOD FOR REFINING SUGAR

1. Система рафинирования сахара-сырца, содержащаяклеровочный узел, выполненный для приема сахара-сырца и растворителя для получения клеровки;узел осветления, выполненный для приема клеровки и получения чистого сиропа; иузел кристаллизации, выполненный для фракционирования высокочистой кристаллической сахарозы из чистого сиропа и получения оттека утфеля;узел умягчения, выполненный для приема оттека утфеля с получением умягченного сиропа;по меньшей мере один узел разделения, выполненный для приема умягченного сиропа с получением продукта с низким содержанием инвертного сахара; ирециркуляционный трубопровод, выполненный для передачи продукта с низким содержанием инвертного сахара из указанного по меньшей мере одного узла разделения в клеровочный узел.2. Система по п. 1, в котором по меньшей мере один узел разделения включает ряд хроматографических колонн, выполненных для приема умягченного сиропа и фракционирования по меньшей мере части инвертных соединений из принятого умягченного сиропа.3. Система по п. 1, в котором указанный по меньшей мере один узел разделения включает:первый ряд хроматографических колонн, выполненных для приема умягченного сиропа и получения промежуточного сахарозного продукта;узел концентрирования для повышения концентрации сухих веществ в промежуточной сахарозе с получением концентрированной сахарозы; ивторой ряд хроматографических колонн, выполненный для приема концентрированной сахарозы и получения продукта с низким содержанием инвертного сахара.4. Система по п. 3, дополнительно содержащая:реактор перекиси водорода, выполненный для приема продукта с низким содержанием инвертного са РОССИЙСКАЯ ФЕДЕРАЦИЯ (19) RU (11) (13) 2014 126 821 A (51) МПК C13B 20/14 (2011.01) ФЕДЕРАЛЬНАЯ СЛУЖБА ПО ИНТЕЛЛЕКТУАЛЬНОЙ СОБСТВЕННОСТИ (12) ЗАЯВКА НА ИЗОБРЕТЕНИЕ (21)(22) Заявка: 2014126821, 27.11.2012 (71) Заявитель(и): АМАЛГАЙМЕЙТЕД РИСЕРЧ ЭлЭлСи (US) Приоритет(ы): (30) Конвенционный приоритет: 02.12.2011 US 61/566,307; 26.11.2012 US 13/684,798 (85) Дата начала ...

Automatic medicine dispensing device based on macro/micro driving and precise liquid medicine control

本发明涉及一种基于宏微驱动和药液精确控制的自动配药装置，属于医疗器械领域。宏微驱动注射器运动单元与光栅尺直线位移传感器形成闭环反馈控制，精确控制注射器注入药袋的位置与注射器注入西林瓶的位置，其中伺服电机经过蜗轮蜗杆减速带动转动块实现注射器90°翻转的动作；机械手抓取西林瓶运动单元也利用宏微结合双重驱动控制丝杠运动将西林瓶从传送带托盘上准确抓取到指定位置的弹簧杯中，并配有消毒喷头给西林瓶口消毒。西林瓶震荡单元在药物注入西林瓶后由电机带动进行特定幅度特定频率的震荡，使药物充分溶解。实现了快速精准的配药，充分利用药物，避免浪费，且可以减轻护士压力，减少配药差错，具有重要的现实意义和实用价值。

Method for white sucrose, brown sucrose and black sucrose production using direct recovery process

본 발명은 사탕수수를 압착 및 착즙하여 사탕수수 원액을 추출하는 압착 및 착즙단계; 상기 원액에 석회를 첨가하고, 이물질과 불순물을 제거하여 건조 물질 기준으로 80 % 이상의 수크로오스 함량의 원액을 제조하는 석회첨가 여과단계; 상기 여과된 원액을 제1 진공농축장치에서 진공농축하여 수크로오스를 포함하는 1차 진공결정슬러리를 제조하는 1차 진공결정단계; 상기 1차 진공결정슬러리를 제1 고속원심분리기에서 원심분리하여 제1 결정과 제1 모액으로 분리하고, 상기 제1 결정으로 삼온당을 제조하거나, 또는 상기 제1 결정을 제2 진공농축장치로 이송시키는 단계; 상기 제2 진공농축장치에서 진공농축하여 수크로오스를 포함하는 2차 진공결정슬러리를 제조하는 2차 진공결정단계; 상기 2차 진공결정슬러리를 제2 고속원심분리기에서 원심분리하여 제2 결정과 제2 모액으로 분리하고, 상기 제2 모액은 상기 압착 및 착즙단계로 이송시키고, 상기 제2 결정은 건조시켜 중백당을 제조하거나 또는 제3 진공농축장치로 이송시키는 단계; 상기 제3 진공농축장치에서 진공농축하여 수크로오스를 포함하는 3차 진공결정슬러리를 제조하는 3차 진공결정단계; 상기 3차 진공결정슬러리를 제3 고속원심분리기에서 원심분리하여 제3 결정과 제3 모액으로 분리하고, 상기 제3 모액을 제1 진공농축장치로 이송시키고, 상기 제3 결정은 건조시켜 정백당을 제조하는 단계를 포함하는 정백당, 중백당 및 삼온당의 제조방법에 관한 것이다. The present invention is a pressing and juice step of extracting the sugar cane juice by squeezing and juice the sugar cane; A lime addition filtration step of adding lime to the stock solution and removing foreign substances and impurities to prepare a stock solution having a sucrose content of 80% or more on a dry matter basis; A primary vacuum crystal step of producing a primary vacuum crystal slurry containing sucrose by vacuum concentrating the filtered stock solution in a first vacuum concentrator; The first vacuum crystal slurry is centrifuged in a first high-speed centrifuge to separate the first crystal and the first mother liquor, and the tricrystalline sugar is produced from the first crystal, or the first crystal is transferred to a second vacuum concentrator. Transferring; A secondary vacuum crystal step of concentrating a vacuum in the second vacuum concentrator to produce a secondary vacuum crystal slurry containing sucrose; The second vacuum crystal slurry is centrifuged in a second high-speed centrifuge to separate the second crystal and the second mother liquor, the second mother liquor is transferred to the pressing and juice step, and the second crystal is dried to give a heavy white sugar. Manufacturing or transferring the same to a third ...

Method of crystallization of sugar-containing solution

Sugar juice evaporation device

一种糖汁蒸发装置，包括有依次连接的一号蒸发罐、二号蒸发罐、三号蒸发罐、四号蒸发罐、五号蒸发罐、六号蒸发罐以及冷凝器，还包括有微滤装置，微滤装置连接在二号蒸发罐和三号蒸发罐之间或者连接在三号蒸发罐和四号蒸发罐之间，所述微滤装置包括依次连接的第一换热器、第一缓冲缸、多级陶瓷膜微滤系统、第二缓冲缸以及第二换热器。本发明设置的多级陶瓷膜微滤系统，可过滤去除糖汁在一效蒸发及二效蒸发产生的沉淀物后再进入三效蒸发浓缩，不仅防止了蒸发过程产生的沉淀物对后序工段的不利影响，还提高了糖浆的质量以及成品糖的品质。

Size distribution controlling crystallizing process

本发明涉及一种优异的粒度分布控制结晶法。该方法避免了现有方法的缺点,采用真空浓缩结晶法使结晶析出时,在结晶母液浓缩过程中,周期性升降浆温度(料温),进行粒度分布控制。

A kind of agricultural irrigation fertilising double-purpose equipment

本发明涉及农业灌溉技术领域，尤其为一种农业灌溉施肥双用设备，包括水塔、水泵、配肥装置和分流管，所述配肥装置包括溶解室、调节室、连接管道、固定箱和调节管道，所述调节室和溶解室通过连接管道上下连通，所述溶解室顶端螺纹连接有肥料箱，且溶解室内侧壁固定连接有过滤层，所述溶解室左端固定连接有调节管道，且调节管道上固定设有第二电水阀和增压泵，所述分流管底端固定连接有土壤酸碱度速测仪，所述分流管右端分支固定连接有输水管，所述输水管底端固定连接有插管，且插管表面开设有透水孔，所述插管底端固定连接有锥形刺，本发明可以实现灌溉和施肥两用效果，结构科学，具有巨大的经济效益和广泛的市场需求，值得推广。