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    • 专利摘要:
    IMPROVED PRE-IMPREGNATION PROCESS FOR CONVERSION OF BIOMASS. The present invention is related to an improved method of conducting a pre-impregnation step, involving the pre-impregnation of lignocellulosic biomass in a liquid (water) at a temperature ranging between 100 “Ca 150 ° C, before impregnation under higher temperatures. This material can then be impregnated and the impregnated liquid filtered through a nanofiltration procedure. When the nanofiltration procedure is used, the pre-impregnation temperature can be in the range of 10 “C to 150 ° C.
    公开号:BR112014016039B1
    申请号:R112014016039-2
    申请日:2012-12-28
    公开日:2020-11-17
    发明作者:Cherchi Francesco；Ottonello Piero；Ferrero Simone；Torre Paolo；De Faveri Danilo；Rivas Torres Beatriz；Tonet Renst Liliane；Riva Daniele；Bosto Federica
    申请人:Beta Renewables S.P.A.；
    IPC主号:
    专利说明:

    Background of the Invention
    [001] Patent document WO 2010/13129 is a Patent Application incorporated herein in its entirety by that reference, which teaches a process for the treatment of lignocellulosic biomass comprising the steps of: (A) impregnating a raw material of lignocellulosic biomass in steam or liquid water, or mixture thereof, in the temperature range of 100 to 210 ° C, for a period of 1 minute to 24 hours, to create an impregnated biomass containing a dry matter content and a first liquid; (B) separating at least a portion of the first liquid from the impregnated biomass to create a first liquid stream and a first solid stream, wherein the first solid stream comprises the impregnated biomass; and (C) steam blasting the first solid stream to create a steam blown stream comprising solids and a second liquid.
    [002] Claim 4 of WO 2010/13129 teaches that the impregnation step (A) can be preceded by a low temperature impregnation step, in which the lignocellulosic biomass is impregnated in a liquid made up of water, at a temperature in the range of 25 to 100 ° C, for a period of 1 minute to 24 hours, and the low temperature impregnation step is followed by a separation step, to separate at least a portion of the liquid from the low temperature impregnation. The document also refers to a process under low temperature.
    [003] What is not disclosed in WO 2010/13129 is the further treatment of currents, or the procedures disclosed in this Patent Application that further improve the steps and processes cited in WO 2010/13129. Summary of the Invention
    [004] This specification discloses a process for the treatment of lignocellulosic biomass, comprising the steps of: A) introducing a liquid stream consisting of water and a feed stream consisting of lignocellulosic biomass solids, containing cellulose and sugars, within a pre-impregnation vessel; B) pre-impregnate the feed stream with the liquid stream at a temperature in the range above 100 ° C-150 ° C; C) separating at least a portion of the liquid stream from the solids, to create a first stream of solid products and a stream of pre-impregnated liquid product; and D) impregnate the first stream of solids according to the following steps: (1) impregnate the stream of solid product in steam or liquid water, or mixture of them, in the temperature range of 100 ° C to 210 ° C, during a period of time in the range of 1 minute to 24 hours, to create a second impregnated biomass, containing a dry matter content and an impregnated liquid; (2) separating at least a portion of the impregnated liquid from the second impregnated biomass to create a stream of impregnated liquid and a second stream of solids, where the second stream of solids comprises the second impregnated biomass.
    [005] It is further disclosed that the weight of sugars in the pre-impregnated liquid stream, in relation to the total weight of lignocellulosic biomass sugars in the feed stream, is less than a value selected from the group consisting of 5% by weight, 2 , 5% by weight and 1% by weight.
    [006] Also, it is also reported that pre-impregnation can be done in less than 48 hours.
    [007] It is further disclosed that the weight ratio of the liquid stream to the supply stream may be less than a selected proportion of the group consisting of 4: 1, 6: 1, 10: 1, 15: 1 and 20: 1.
    [008] An additional stage of filtration of the impregnated liquid stream can be done by nanofiltration.
    [009] It is further disclosed that the impregnated liquid has an instantaneous flow greater than 7 L / h-m2, where the instantaneous flow is a flow that occurs when the volume of 72L of a fraction of 190L of at least a portion of the impregnated liquid has passed through a spiral nanofilter membrane, where the specification of the membrane is a type of polyamide thin film composed of polyester, with a magnesium sulfate rejection greater than or equal to 98% when measured at 2000 ppm of magnesium sulfate in water, at a pressure of 9 bar and a temperature of 25 ° C, and having an external diameter of 64.0 to 65.0 mm, a length of 432 mm and an internal diameter of 21 mm, the membrane having a cross flow of 1.3-1.8 m3 / h, with a maximum pressure drop of 0.6 bar, in viscosity of 1 cP, and a membrane model area of 0.7 m2.
    [010] It is further reported that the spiral nanofilter membrane is designed according to the 2011 filter specification, model NF99, available from Alfa Lavai (Sweden), or that the spiral nanofilter membrane is actually the membrane model NF99 , available from Alfa Lavai (Sweden), as provided by Alfa Lavai in 2011.
    [011] It is also reported that the separation of at least a portion of the acetic acid is done by nanofiltration.
    [012] It is further disclosed that when nanofiltration is used or that the flow is present, the following process can be used with all the variations disclosed above. A) Introduce a liquid stream made up of water and a feed stream made up of lignocellulosic biomass solids, containing cellulose, glycans and xylans, into a pre-impregnation vessel; B) pre-impregnate the feed stream with the liquid stream at a temperature in the range of 10 ° C to 150 ° C; C) separating at least a portion of the liquid stream from the solids, to create a first stream of solid products and a stream of pre-impregnated liquid product; and D) treating the first stream of solids with an impregnation step, comprising the following steps: (1) impregnating the first stream of solids in steam or liquid water, or mixture thereof, in the temperature range of 100 ° C to 210 ° C ° C, to create a second impregnated biomass, containing a dry matter content and an impregnated liquid; (2) separating at least a portion of the impregnated liquid from the second impregnated biomass to create a stream of impregnated liquid consisting of suspended solids, monomeric sugar, oligomeric sugars, acetic and furfural acid, and a second stream of solids, in which the second solid stream comprises the second impregnated biomass; E) separating at least a portion of the impregnated liquid from the suspended solids of the impregnated liquid stream comprising monomeric sugars, oligomeric sugars, acetic and furfural acid; and F) filtering at least a portion of the acetic acid from at least a portion of the impregnated liquid, in order to create a permeate (permeate solution) and a retentate (retained solution).
    [013] It is also disclosed that the feed stream can be pre-impregnated with the liquid stream at a temperature in the range of 10 ° C to 100 ° C, while being exposed to a vacuum condition and in which the vacuum condition can be less than an absolute pressure measured in millibar (mbar), selected from the group consisting of 950, 900, 850, 800, 700, 600, 500, 400, 300, 250, 200, 150, 100, 50, 30, 20, 10, 5 and 0.5 mBar. Brief Description of the Figures
    [014] In the attached figures: figure 1 presents two schematic routes, showing the state of the art and a modality of the process proposed by the invention; figure 2 shows the composition of the impregnated liquid, with and without the pre-impregnation step; - figure 3 shows the composition of the steam-blown solids, with and without the pre-impregnation step; figure 4 shows the flow of the impregnated liquid stream from each experiment, as a function of time; Figure 5 shows the flow of the impregnated liquid stream from each experiment, expressed as a function of the volume of permeate solution passed through the filter; and figure 6 shows the comparison of results of pre-impregnation experiments, carried out with and without exposure of the lignocellulosic biomass to a vacuum condition, during the pre-impregnation treatment. Description of the Invention
    [015] The present invention is based on the discovery that the maximum temperature of a first pre-impregnation step, before the impregnation pre-treatment which may or may not be followed by a steam explosion, is the temperature at which the hemicellulose solubilizes in lignocellulosic biomass. This temperature is highly variable and depends on the type of lignocellulosic biomass, with respect to the amount of time the lignocellulosic biomass is maintained at that temperature.
    [016] Patent document WO 2010/13129 teaches a pre-impregnation step, but it also teaches that the low temperature of the first pre-impregnation step must be between 25 ° C and 100 ° C. This indication is distant and different from that of temperatures higher than 100 ° C. Temperatures above 100 ° C require pressure vessels, special heating kits, insulation, and increased operating and capital costs for the process in question.
    [017] It was also discovered that after impregnation below the hemicellulose solubility temperature, the filterability of the liquid removed is markedly enhanced when measured by the increase in the life of the filter. The pre-impregnation step at a higher temperature removes the critical buffering compounds from the filter, so that the liquid purification step after the impregnation hydrolysis step needs to use only one unit operation, such as a filter (for example , type of nanofiltration, instead of two unit operations in series (for example, ultrafiltration, followed by nanofiltrations). The process may feature a centrifuge filter and / or a bag filter, for filtration of 1 micron size or more, before the nanofiltration step, so that expensive ultrafiltration is avoided, and the process can be operated free of ultrafiltration.
    [018] Therefore, the application of an improvement in the process cited by the patent document WO 2010/13129 is that pre-impregnation does not have to be done at a low temperature, instead, it can be done in the temperature range between 100 ° C and 150 ° C, not including 100 ° C, which is the upper temperature limit mentioned in WO 2010/13129.
    [019] It has been noted that higher temperatures work more satisfactorily to remove contaminants, particularly contaminants that inhibit liquid nanofiltration in the impregnation step (not in the pre-impregnation step).
    [020] The lignocellulosic biomass useful for the present process can be characterized as follows. First, in addition to starch, the three main constituents in plant biomass are cellulose, hemicellulose and lignin, which are commonly referred to by the generic term lignocellulose. Biomasses containing polysaccharides as a generic term, include starch biomasses and lignocellulosic biomasses. Therefore, some types of raw materials may include plant biomass, biomass containing polysaccharides and lignocellulosic biomass.
    [021] The biomasses containing polysaccharides according to the present invention include any material containing polymeric sugars, for example, in the form of starch, as well as refined starch, cellulose and hemicellulose.
    [022] Relevant types of biomass to give rise to the claimed invention may include biomass derived from agricultural crops, selected from the group consisting of grains containing starch, refined starch; corn straw, bagasse, and straw, for example, rice, wheat, rye, oats, barley, rapeseed, sorghum; coniferous wood, for example, Pinus sylvestris, Pinus radiate; common wood, for example, Salix spp. Eucalyptus spp .; tubers, for example, beets, potatoes; cereals originating from, for example, rice, wheat, rye, oats, barley, rapeseed, sorghum and maize crops; residual paper, fibrous fractions from biogas processing, fertilizer, palm oil processing residues, municipal solid waste, or similar materials. Although the experiments are limited to a few examples from the list enumerated above, the invention is believed to be applicable to all examples cited, due to the fact that the characterization is mainly for the unique characteristics of lignin and surface area.
    [023] The raw material of lignocellulosic biomass used in the present process is preferably from the family normally called grasses. The appropriate name is the family known as Poaceae or Gramineae, of the Liliopsida Class (the monocotyledons) of flowering plants. The plants of this family are usually called grasses or, to differentiate it from other grasses, real grasses. Bamboo is also included. The existence of approximately 600 genera and about 9,000-10,000 or more species of grass is known (Kew Index of World Grass Species).
    [024] The Poaceae family includes the main food grains and cereal crops grown around the world, grass and forage grasses, and bamboo. The Poaceae family usually has hollow stems called stems, which are covered (made solid) at intervals called nodes, the points along the stalk at which the leaves appear. The leaves of the grass are usually alternating, distal (in a plane) or rarely spiral and with parallel veins. Each leaf is distinguished by a lower sheath, which narrows the stem by a certain distance and a blade with a normally entire edge. The leaf blades of many grasses are hardened with silica phytoliths, which help to discourage animal grazing. In some grasses (for example, sword-like grasses), this makes the edges of grass blades sharp enough to cut human skin. A membranous attachment or fringe of hair, called a ligula, is provided at the junction between the sheath and the blade, which prevents water or insects from entering the sheath.
    [025] Blades of grass grow from the base of the blade and not from elongated tips of the stem. This low growth point is evolved in response to grazing animals and allows grasses to be used for grazing or trimmed regularly, without causing severe damage to plants.
    [026] The flowers of the Poaceae are typically arranged on ears, each ear having one or more florets (the ears are still grouped into panicles or long clusters). An ear consists of two (or sometimes less) bracts at the base, called glumes, followed by one or more florets. A little flower consists of the flower surrounded by two bracts called the lemma (the outer bract) and the pale (the inner). Flowers are usually hermaphroditic (corn, monoecia is an exception) and pollination is almost always anemophilous. The perianth is reduced to two scales, called mudflats, which expand and contract to spray the motto and the pallea; these are generally interpreted as modified sepals.
    [027] The fruit of the Poaceae is a caryopsis in which the seed cover is fused to the fruit wall and thus cannot be separated from it (as in the case of a corn pit).
    [028] There are three general classifications of growth habit present in grasses; bunch type (also called cespitose), stoloniferous and rhizomatous.
    [029] The success of grasses lies, in part, in their morphology and growth processes, and in part, in their physiological diversity. Most grasses are divided into two physiological groups, using the C3 and C4 photosynthetic pathways for carbon fixation. Type C4 grasses have a photosynthetic path linked to the special anatomy of the Kranz leaf, which particularly adapts them to hot climates and an atmosphere with a low carbon dioxide content.
    [030] Type C3 grasses are referred to as "cold season grasses", while type C4 plants are considered "hot season grasses". Grass can be annual or perennial. Examples of annual cold season grasses include wheat, rye, annual bluegrass (also called field grass), (annual meadow grass, grass of the genus Poa and annual oats). Examples of perennial cold season grasses include orchid grass (rooster foot, Dactylis glomerata), fescue (Festuca spp), Kentucky bluegrass and perennial rye grass (Lolium perenne). Examples of annual hot season grasses include maize, Sudan grass and millet. Examples of perennial hot season grasses include large blue stem grasses, Indian grasses, shorts grass and switchgrass.
    [031] A classification of the grass family recognizes twelve subfamilies: these are: 1) ano-mochlooideae, a small line of broad-leaved grasses, which includes two genera (Anomochloa, Streptochaeta); 2) Pharoideae, a small strain of grass that includes three genera, including Pharus and Leptaspis; 3) Puelioideae, a small strain that includes the African Puelia genus; 4) Pooideae, which includes wheat grasses, barley, oats, and bromine grass (Bronnus) and kingdom cane grams (Calamagrostis); 5) Bambusoideae, which includes bamboo; 6) Ehrhartodeae, which includes rice and wild rice; 7) Arundinoideae, which includes cane from the giant kingdom and cane from the common kingdom; 8) Centothecoideae, a small subfamily of 11 genera that is sometimes included in the family Panicoideae; 9) Chloridoideae, including lovegrasses grasses (Eragrostis, approximately 350 species, including Tef grain), dropseeds (Sporobolus, about 160 species), millet (finger millet) (Eleusine coracana (L.) Gaertn.), and muhly grasses (Muhlenbergia, about 175 species); 10) Panicoideae, including panic grass, and grasses of corn, sorghum, sugar cane, of larger millets, and grasses of phonon type and blue stem; 11) Micrairoideae; 12) Danthoniodieae, including pampas grass; with grass of the genus Poá, which is a genus of about 500 species of native grasses, in temperate regions of both hemispheres.
    [032] Agricultural grasses that are grown to remove edible seeds are called cereals. The most common cereals are rice, wheat and corn. Of all cultures, 70% are grasses.
    [033] Sugarcane is the main source of sugar production. Grasses are used for construction. Scaffolding materials made from bamboo are also able to withstand typhoon winds that could break steel scaffolding. Larger bamboo and the Arundo donax species have robust stems that can be used in a similar way to wooden logs, and the grass roots stabilize the grassy land of grassy land houses. The Arundo species is used to make reeds for wind instruments and bamboo is used for countless implements.
    [034] Therefore a preferred lignocellulosic biomass can be selected from the group consisting of grasses and wood. A preferred lignocellulosic biomass can be selected from the group consisting of plants belonging to coniferous species, angiosperms, and families of Poaceae and / or Gramineae. Another preferred lignocellulosic biomass can also be that biomass having at least 10% by weight of its dry matter content in the form of cellulose or, more preferably, at least 5% by weight of its dry matter content in the form of cellulose.
    [035] Lignocellulosic biomass will also comprise carbohydrate (s), selected from the group of carbohydrates based on glucose, xylose and mannose monomers. Derived from lignocellulosic biomass means that the lignocellulosic biomass in the feed stream will comprise glycans, xylans and lignin.
    [036] The raw material for lignocellulosic biomass may also originate from woody plants. A woody plant is a plant that uses wood as its structural fabric. These are typically perennial plants, whose larger stems and roots are reinforced with wood produced adjacent to vascular tissues. The main stem, the largest branches and roots of these plants are usually covered by a thicker layer of bark. Woody plants are usually trees, shrubs or vines. Wood is a structural cell adaptation that allows woody plants to grow above the trunks of the soil, year after year, thereby making woody plants the largest and tallest plants.
    [037] These plants need a vascular system to move water and nutrients from the roots to the leaves (xylem) and to move sugars from the leaves to the rest of the plant (phloem). There are two types of xylem: the primary xylem, which is formed during the primary growth of the procambium, and the secondary xylem which is formed during the secondary growth of the vascular exchange.
    [038] What is usually called "wood" is the secondary xylem of these plants.
    [039] The two main groups in which the secondary xylem can be found are: 1) Conifers (Coniferae) - there are about 600 species of conifers. All species have secondary xylem, which is relatively uniform in structure throughout this group. Many conifers become tall trees: the secondary xylem of these trees is marketed as coniferous wood. 2) Angiosperms (Angiospermae) - there are about two hundred and fifty thousand to four hundred thousand species of angiosperms. Within this group, secondary xylem was not found in monocotyledons (for example, Poaceae). Many non-monocotyledon angiosperms become trees and their secondary xylem is marketed as hardwood.
    [040] The term coniferous wood is used to describe the wood of trees that belong to the family of gymnosperms. Gymnosperms are plants with uncovered seeds not included in an ovary. These seed "fruits" are considered more primitive than hardwood. Coniferous wood trees are usually perennial, bear cones and have needle-like or scale-like leaves. They include coniferous species, for example, pine, spruce, other types of pine and cedar. The hardness of the wood varies between coniferous species.
    [041] The term hardwood is used to describe the wood of trees that belong to the family of angiosperms. Angiosperms are plants with eggs included for protection in an ovary. When fertilized, these eggs develop into seeds. Hardwood trees are usually wide-spread; in temperate and boreal latitudes they are mainly deciduous, but in the tropics and sub-tropics they are mainly perennial. These leaves can be simple (single slides) or they can be composed with leaves attached to the leaf stem. Although variable in shape, all the leaves of hardwood plants have different networks of thin veins. Hardwood plants include, for example, black beech, birch, cherry, tree of the Aceraceous family, oak and wood of Indian origin.
    [042] Glycans include glycan monomers, dimers, oligomers and polymers in lignocellulosic biomass. Of particular interest is 1,4-beta-glycan, which is specific for cellulose, instead of 1,4-alpha-glycan. The amount of 1,4-beta-glycan present in the previously treated lignocellulosic biomass must be at least 5% by weight of the previously treated lignocellulosic biomass, based on the dry content, more preferably, at least 15% by weight of previously treated lignocellulosic biomass, based on dry content.
    [043] Xylans include xylan monomers, dimers, oligomers and polymers in the pre-treated lignocellulosic biomass composition.
    [044] While the previously treated lignocellulosic biomass can be starch-free, substantially starch-free, or have a starch content of 0% by weight, or be totally starch-free. The starch, if present, can be less than 75% by weight of the dryness content. There is no preferred starch band, as its presence is not believed to affect glucose hydrolysis. The ranges for the amount of starch, if present, are between 0 and 75% by weight of dryness content, between 0 and 50% by weight of dryness content, between 0 and 30% by weight of dryness content and between 0 and 25% by weight of dryness content.
    [045] Because the invention is directed towards the hydrolysis of glucose, the specification of the invention and the present inventors believe that any lignocellulosic biomass with 1,4-beta-glycans can be used as raw material for the present improved process of hydrolysis.
    [046] The pretreatment used in lignocellulosic biomass can be any pretreatment known in the prior art and any of those to be invented in the future.
    [047] The pre-treatment used to previously treat the previously treated lignocellulosic biomass is used to ensure that the structure of the lignocellulose content is made more accessible to catalysts, such as enzymes, and that, at the same time, the concentrations of by-products health hazard inhibitors such as acetic, furfural and hydroxymethylfurfural remain substantially low.
    [048] Current pre-treatment strategies include submitting lignocellulosic material to temperatures between 110-250 ° C, for a period of 1-60 minutes, for example: - extraction under hot water; - multi-stage diluted acid hydrolysis, which removes dissolved material, before inhibitory substances are formed; - hydrolysis of the diluted acid under relatively low gravity conditions; - alkaline to wet oxidation; - steam explosion; - any pre-treatment with subsequent detoxification.
    [049] If a hydrothermal pretreatment is chosen, the following conditions are preferred: pretreatment temperature: 110-250 ° C, preferably 120-240 ° C, more preferably 130-230 ° C, more preferably still , 140-220 ° C, even more preferably, 150-210 ° C, more preferably, 160-200 ° C, even more preferably, 170-200 ° C or even more preferably, 180-200 ° C. - pre-treatment time: 1-60 minutes, preferably 2-55 minutes, more preferably 3-50 minutes, more preferably preferably 4-45 minutes, even more preferably 5-40 minutes, more preferably 5- 35 minutes, even more preferably, 5-30 minutes, even more preferably, 5-25 minutes, more preferably, 5-20 minutes and even more preferably, 5-15 minutes.
    [050] The dry matter content after pre-treatment is preferably at least 20% (weight / weight). Other preferable upper limits are contemplated, as the amount of biomass for water in the previously treated lignocellulosic raw material is available in the 1: 4 to 9: 1 proportion ranges; 1: 3.9 to 9: 1, 1: 3.5 to 9: 1, 1: 3.25 to 9: 1, 1: 3 to 9: 1, 1: 2.9 to 9: 1, 1: 2 to 9: 1, 1.15 to 9: 1, 1: 1 to 9: 1, and 1: 0.9 to 9: 1.
    [051] The biomasses containing polysaccharides according to the present invention include any material containing polymeric sugars, for example, in the form of starch, as well as refined starch, cellulose and hemicellulose. However, as discussed earlier, starch is not a major component.
    [052] A preferred pre-treatment process is the two-stage impregnation / extraction process, followed by a steam explosion, as described below.
    [053] A preferred pretreatment of a lignocellulosic biomass includes a pre-impregnation of the lignocellulosic biomass feedstock and a steam explosion of at least part of the impregnated lignocellulosic biomass feedstock.
    [054] Impregnation occurs in a substance, such as water in the form of steam, or in the form of liquid, or liquid and steam together, to produce a product. The product is an impregnated biomass containing an impregnating liquid, wherein the impregnating liquid is usually water in its liquid state, or steam, or some mixture.
    [055] This impregnation can be done by any number of techniques that expose a substance to water, which can be in the form of steam or in liquid form, or a mixture of steam and water or, more generally, to water at a high temperature and high pressure. The temperature can be found in one of the following ranges: 145 to 165 ° C, 120 to 210 ° C, 140 to 210 ° C, 150 to 200 ° C, 155 to 185 ° C, 160 to 180 ° C. Although the time can be extended, such as, up to, but less than 24 hours, or less than 16 hours, or less than 12 hours, or less than 9 hours, or less than 6 hours, the exposure time is preferably it is quite short, ranging from 1 minute to 6 hours, from 1 minute to 4 hours, from 1 minute to 4 hours, from 1 minute to 3 hours, from 1 minute to 2.5 hours, more preferably, from 5 minutes to 1 , 5 hours, 5 minutes to 1 hour, or 15 minutes to 1 hour.
    [056] If steam is used, it should preferably be saturated, but it can be overheated. The impregnation step can be batchwise or continuous, with or without agitation. A low temperature impregnation before high temperature impregnation can be used. The temperature of the impregnation under low temperature is in the range of 25 to 90 ° C. Although the time can be extended, such as up to, however, less than 24 hours, or less than 16 hours, or less than 12 hours, or less than 9 hours, or less than 6 hours, the exposure time is preferably rather short, ranging from 1 minute to 6 hours, from 1 minute to 4 hours, from 1 minute to 4 hours, from 1 minute to 2.5 hours, more preferably, from 5 minutes to 1.5 hours, from 5 minutes to 1 hour, or 15 minutes to 1 hour.
    [057] Each impregnation step may also include the addition of other compounds, for example, H2SO4, NH3, in order to obtain a greater performance in the process.
    [058] The product comprising the impregnation liquid, or the impregnated liquid is then passed to a separation step, where said at least a portion of the impregnation liquid is separated from the impregnated biomass. The liquid will not separate completely, so that at least a portion of the impregnation liquid is separated, preferably with as much impregnation liquid as possible in a time-saving structure. The liquid from this separation step is known as an impregnated liquid stream, comprising the impregnating liquid. The impregnated liquid will be the liquid to be used in the impregnation, generally, water and the soluble fractions of the raw material. Such water-soluble fractions include glycan, xylan, galactan, arabinan, glyco-oligomers, xylo-oligomers, galacto-oligomers and arabinoligomers. Solid biomass is called the first stream of solids, as it contains most, if not all, solids.
    [059] The separation of the impregnated liquid can, again, be done by means of known techniques and, probably, some that have not yet been invented. A preferred piece of equipment is a press, as the press will generate a liquid under high pressure.
    [060] The first solid stream can optionally be then steam blown to create a steam blown stream comprising solids. The steam explosion is a well-known technique in the field of biomass and any systems available today and in the future are believed to be suitable for this step.
    [061] The rigor of the steam explosion is known in the literature as (Ro), being a function of time and temperature, and being expressed by: Ro = texp [(T-100) / 14.75] with temperature (T) expressed in ° C and the time (t) expressed in minutes.
    [062] The formula is also expressed as Log (Ro), namely: Log (Ro) = Ln (t) + [(T-100) / 14.75]. Log (Ro), preferably, ranges within the ranges of 2.8 to 5.3; 3 to 5.3; 3 to 5.0; and 3 to 4.3.
    [063] The steam blown chain can optionally be washed with at least water and other additives can also be used. It is conceivable that another liquid could be used in the future, so that water is not considered to be absolutely essential. In this respect, water is the preferred liquid. The liquid effluent from the optional washing is the third liquid stream. This washing step is not considered essential, and is therefore optional.
    [064] The exploded washed stream is then processed to remove at least a portion of the liquid in the exploded washed material. This separation step is also optional. The expression "at least a portion is removed" means that while the greatest possible removal of liquid is desirable (preferably by pressing), 100% removal is unlikely to be possible. In any case, 100% water removal is not desirable, since water is necessary for the subsequent hydrolysis reaction. The preferred process for this step is again referred to as the pressing procedure, but other known techniques and those that have not yet been invented are believed to be suitable. The products separated from this process are solids in the second stream of solids and liquids in the second stream of liquid.
    [065] One aspect of the invention includes exposing lignocellulosic biomass to a pre-impregnation step, prior to an impregnation step, in a temperature range between 100 ° C and 150 ° C, where the term "between" means that temperatures of 100 ° C and 150 ° C are not included. The temperature range of 105 ° C to 150 ° C, which includes 105 ° C and 150 ° C is also a preferred range. A temperature in the range of 110 ° C to 150 ° C is also considered to fall within a preferred range. Also, a temperature range between 100 ° C and 145 ° C is contemplated. The temperature range of 105 ° C to 145 ° C, which includes 105 ° C and 145 ° C is also a preferred range. A temperature in the range of 110 ° C to 145 ° C is also considered to fall within a preferred range.
    [066] The pre-impregnation time can be extended, such as, up to, however, less than 48 hours, or less than 24 hours, or less than 16 hours, or less than 12 hours, or less than 9 hours, or less than 6 hours; the exposure time is preferably very short, ranging from 1 minute to 6 hours, from 1 minute to 4 hours, from 1 minute to 4 hours, from 1 minute to 3 hours, from 1 minute to 2.5 hours, more preferably, from 5 minutes to 1.5 hours, from 5 minutes to 1 hour, or from 15 minutes to 1 hour.
    [067] In one embodiment, the lignocellulosic biomass is subjected to a vacuum condition during submission to the pre-impregnation treatment. The prepreg treatment is carried out at a temperature greater than 10 ° C and preferably less than 100 ° C, more preferably less than 90 ° C, even more preferably less than 80 ° C, more preferably still less at 70 ° C, with a temperature below 60 ° C being the most preferred temperature. The present inventors have found that exposure to the vacuum condition increases the amount of material that is removed from the lignocellulosic biomass during the pre-impregnation treatment. The vacuum condition can occur for a vacuum exposure time that is equal to or less than the prepreg time, preferably less than the prepreg time, more preferably less than 90% of the prepreg time, still more preferably less than 80% of the prepreg time, more preferably less than 60% of the prepreg time, even more preferably less than 50% of the prepreg time, 40% of the time pre-impregnation is the most preferred value. In one embodiment, the vacuum exposure time can be longer than the pre-impregnation time, as can occur in the case where the exposure of the lignocellulosic biomass to the vacuum condition is established before starting the pre-impregnation treatment, or in the event that the exposure of the lignocellulosic biomass to the vacuum condition is interrupted after the end of the pre-impregnation treatment.
    [068] The vacuum condition is lower than atmospheric pressure, which is an absolute pressure measured in millibar (mbar), less than 1013.25 millibar, and can be selected from the group consisting of 950, 900, 850, 800, 700 , 600, 500, 400, 300, 250, 200, 150, 100, 50, 30, 20, 10, 5, and 0.5 mbar.
    [069] The pre-impregnation step is done in the presence of a liquid, which is the impregnated liquid. After impregnation, this liquid was preferably removed by less than 5% by weight with respect to the total weight of sugars in the raw material, more preferably by less than 2.5% by weight with respect to the total weight of sugars in the raw material, with more preferred, less than 1% by weight with respect to the total weight of sugars in the raw material. This pre-impregnation step is useful as a modification of a pre-treatment step for biomass. In the impregnation (not in the pre-impregnation) of the biomass pre-treatment steps, the impregnated liquid that has been separated from the impregnated solids, preferably, will have reduced the filter buffer components, so that the impregnated liquid can be easily nanofiltered. A property of the impregnated liquid is that it can have an instantaneous flow greater than 7 L / h-m2, where the instantaneous flow is a flow that occurs when the 72L volume of a 190L fraction of at least a portion of the impregnated liquid has passed through a spiral nanofilter membrane, where the specification of the membrane is a type of polyamide thin film composed of polyester, with a magnesium sulfate rejection greater than or equal to 98% when measured at 2000 ppm of magnesium sulfate in water, at a pressure of 9 bar and a temperature of 25 ° C, and having an external diameter of 64.0 to 65.0 mm, a length of 432 mm and an internal diameter of 21 mm, the membrane having a cross flow of 1.3-1.8 m3 / h, with a maximum pressure drop of 0.6 bar, in viscosity of 1 cP, and a membrane model area of 0.7 m.
    [070] Although an instantaneous flow greater than 7 is preferred, according to the method described, the instantaneous flow can be greater than a value selected from a group consisting of 7, 8, 9, 10 and 15.
    [071] When compared to the nanofiltration step, the pre-impregnation temperature can be increased to the range of 10 ° C to 150 ° C, more preferably, 25 ° C to 150 ° C, even more preferably, 25 ° C to 145 ° C, with 25 ° C to 100 ° C and 25 ° C to 90 ° C also being preferred ranges. Experiments
    [072] A comparison between three experiments is presented.
    [073] The raw material is wheat straw and Arundo Donax.
    [074] The compositions were classified in terms of water-soluble components (WS) and water-insoluble components (WIS), with the individual details being presented in Table 1 (List of Components).


    [075] Water-soluble components (WS) have been classified as soluble sugars, known soluble components and unknown soluble components.
    [076] Soluble sugars include glucose, xylose, glyco-oligomers and xylo-oligomers.
    [077] Known soluble components mean components from the following list: acetic acid, hydroxymethylfurfural (HMF), furfural, salts and ashes.
    [078] Unknown soluble components mean all soluble components other than sugars and known soluble components.
    [079] Water insoluble components (WIS) have been classified as insoluble sugars, known insoluble components and unknown insoluble components.
    [080] Insoluble sugars include glycans and xylans.
    [081] Known insoluble components mean insoluble acetyl groups.
    [082] Unknown insoluble components mean all insoluble components other than known insoluble sugars and insoluble components.
    [083] Analytical measurements were performed according to the following NREL Standard Analytical Methods. Determination of the Structure of Carbohydrates and Lignin in Biomass Laboratory Analytical Procedure (LAP); Publication Date: 04/25/2008. Technical Report NREL / TP-510-42618; Revised in April 2008. Determination of Extractives in Biomass Laboratory Analytical Procedure (LAP); Publication Date: 07/17/2005. Technical Report NREL / TP-510-42619; January 2008. Sample Preparation for Analysis of Composition Laboratory Analytical Procedure (LAP); Publication Date: 09/28/2005. Technical Report NREL / TP-510-42620; January 2008. Determination of Total Solids in Biomass and Total Solids Dissolved in Liquid Process Samples Laboratory Analytical Procedure (LAP); Publication Date: 03/31/2008. Technical Report NREL / TP-510-42621; Revised in March of Determination of Ash in Biomass Laboratory Analytical Procedure (LAP); Publication Date: 07/17/2005. Technical Report NREL / TP-510-42622; January 2008. Determination of Sugars, By-Products and Decomposition Products in Liquid Fraction Process Samples Analytical Laboratory Procedure (LAP); Publication Date: 08/12/2006. Technical Report NREL / TP-510-42623; January 2008. Determination of Insoluble Solids in the Pre-treated Biomass Material Laboratory Analytical Procedure (LAP); Publication Date: 03/21/2008. Technical Report NREL / TP-510-42627; March 2008. Experiment 1 (Control)
    [084] A quantity of 23 kg of wheat straw based on dry content was introduced into a continuous reactor and subjected to an impregnation treatment at a temperature of 155 ° C for 65 minutes. The impregnated mixture was separated into an impregnated liquid and a fraction containing the raw material impregnated with solid by means of a press. The fraction containing the raw material impregnated with solid was subjected to steam explosion, at a temperature of 190 ° C, for a period of time of 4 minutes.
    [085] The steam blown products were separated into a stream of blown liquid and a stream of blown solid. Experiment 2
    [086] A quantity of 22 kg of wheat straw based on dry content was introduced into a continuous reactor with water in a ratio of 1: 3 and subjected to a prepreg treatment at a temperature of 130 ° C for 30 minutes .
    [087] After pre-impregnation, a pre-impregnated liquid was separated from the pre-impregnated raw material by means of a press.
    [088] The pre-impregnated raw material was subjected to impregnation and steam explosion treatments, as described in Experiment 1. Experiment 3
    [089] A quantity of 22 kg of wheat straw based on dry content was introduced into a batch reactor with water, in a proportion of 1:16, and subjected to a pre-impregnation treatment at a temperature of 65 ° C for 3 hours. The mixture was continuously stirred during the pre-impregnation step.
    [090] After pre-impregnation, a pre-impregnated liquid was separated from the pre-impregnated raw material by means of a press.
    [091] The pre-impregnated raw material was subjected to impregnation and steam explosion treatments, as described in Experiment 1. Results
    [092] Table 2 presents the compositions of raw material (lignocellulosic biomass, for example, wheat straw) from Experiment 1, and also of the raw material, pre-impregnated liquid and pre-impregnated raw material from Experiments 2 and 3.

    [093] Table 2 also contains the percentage content of pre-impregnated liquid in relation to the weight of raw material in sugars, other components, unknown components and volatile components. Table 2 also contains the percentage of sugars in the pre-impregnated liquid, in relation to the amount of sugars in the raw material.
    [094] The pre-impregnation of Experiments 2 and 3 removes 4.5% and 11.2% by weight in relation to the total weight of the raw materials. In Experiment 2, conducted at a temperature higher than that of Experiment 3, volatile components of 0.68 kg of unknown products were also present. Experiment 2 removes 0.3% by weight of the sugars contained in the raw material, which corresponds to 0.6% of the weight of the sugars contained in the raw material. Experiment 3 removes 0.5% by weight of the sugars contained in the raw material, which corresponds to 0.8% of the weight of the sugars contained in the raw material.
    [095] Table 3 contains the composition of impregnated liquid after the impregnation step of Experiments 1 to 3, including the percentage content based on the dry content of known soluble components, unknown soluble components, insoluble components, acetic acid, monomeric sugars and oligomeric sugars. Acetic acid was inserted into the Table separately from the known soluble components. Table 3 - Composition of the Impregnation Liquid

    [096] Figure 2 contains a bar graph of the liquid impregnated composition of Experiments 1 to 3.
    [097] Table 4 contains the composition of steam-blown solids from Experiments 1 to 3, including the percentage content based on the dry content of known soluble components, unknown soluble components, monomeric sugars and oligomeric sugars and insoluble sugars. Table 4 - Composition of Steam Exploded Solids

    [098] Figure 3 contains a bar graph of the steam-blown solids composition from Experiments 1 to 3. Experiment 4
    [099] Experiment 4 was conducted to determine the filterability of the impregnated liquids produced in Experiments 1 to 3.
    [100] The impregnated liquids were subjected to a preliminary stage of prior separation to remove the solids, by means of centrifugation and macrofiltration (bag filter with 1 micron filter mesh size). The centrifugation was performed using an Alfa Lavai centrifuge, model CLARA 80, under a rotation of 8,000 rpm.
    [0101] The previously separated liquids were subjected to nanofiltration using Alfa Lavai 2.5 "equipment (membrane code NF99 2517/48), according to the following procedure.
    [0102] The stability of the permeate flow was verified by means of discharge with demineralized water, at room temperature (25 ° C) and pressure of 4 bar. The permeate flow was measured. A quantity of 192 liters of impregnated liquid was inserted into the feed tank. Before the test, the system was discharged for 5 minutes, without pressure action, in order to remove the water.
    [0103] The system was established under the following operating conditions (pressure: 25-30 bar, temperature: 30 - 35 ° C).
    [0104] The retained material stream was recycled in the feed tank and the permeate stream was damped.
    [0105] The test was processed until the volume of liquid in the feed tank was reduced to up to 62.5% of the initial liquid volume impregnated, corresponding to 72 liters of permeate material and 120 liters of retentate material.
    [0106] The permeate material and the nanofiltrated retentate material were collected.
    [0107] Figure 4 contains the graph of the instantaneous permeate flow, from the impregnated liquids previously separated, along the nanofiltration system, as a function of time. The impregnated liquids from the pre-impregnated raw materials in experiments 2 and 3 show an instantaneous flow greater than that of the impregnated liquid in experiments 1, and the time required to filter a specific volume is reduced.
    [0108] Figure 5 shows the graph of the instantaneous flow of the permeate material from the impregnated liquids previously separated, along the nanofiltration system, depending on the volume of permeate generated. The impregnated liquids from the pre-impregnated raw materials in experiments 2 and 3 have an instantaneous flow greater than that of the impregnated liquid in experiments 1, and the time required to filter a specific volume is reduced.
    [0109] The experiments highlight that by introducing a pre-impregnation step, it is possible to filter a certain amount of liquid in a shorter time, obtaining a greater flow. As a result, the complexity and costs of the filtration system required in an industrial application are considerably reduced. Experiment 5
    [0110] A quantity of 2 kg of Arundo Donax based on dry content was introduced into a vacuum batch reactor (Rotavapor) with water, in a ratio of 1: 6, and subjected to a pre-impregnation treatment at a temperature of 50 ° C, for 30 minutes, and under a pressure of 1 bar. The mixture was continuously stirred during the pre-impregnation step.
    [0111] The same amount of Arundo Donax was subjected to the pre-impregnation treatment under the same conditions, but, being exposed to a vacuum of 0.25 bar.
    [0112] After the pre-impregnation step, a pre-impregnated liquid was separated from the pre-impregnated raw material by means of a press.
    [0113] Pre-impregnated liquids contained irrelevant amounts of sugars in both cases.
    [0114] The percentage by weight of the total components and extractive components removed from the raw material increases significantly in the case of vacuum pre-impregnation, as shown in figure 6. The experiment demonstrates that the exposure of the raw material to vacuum during pre-impregnation treatment it improves the removal of unwanted components, without affecting the removal of sugars.
    权利要求:
    Claims (6)
    [0001]
    1. Process for the treatment of lignocellulosic biomass, characterized by the fact that it comprises the steps of: A) introducing a liquid stream consisting of water and a feed stream consisting of lignocellulosic biomass solids, containing cellulose and sugars, inside a vessel of pre-impregnation; B) pre-impregnate the feed stream with the liquid stream at a temperature in the range above 100 ° C-150 ° C; C) separating at least a portion of the liquid stream from the solids, to create a first stream of solid products and a stream of pre-impregnated liquid product; and D) impregnate the first stream of solids according to the following steps: 1) impregnate the stream of solid product in steam or liquid water, or mixture of them, in the temperature range of 100 ° C to 210 ° C, for a period of period of time in the range of 1 minute to 24 hours, to create a second impregnated biomass, containing a dry matter content and an impregnated liquid; 2) separating at least a portion of the impregnated liquid from the second impregnated biomass to create an impregnated liquid stream and a second solid stream, where the second solid stream comprises the second impregnated biomass.
    [0002]
    2. Process according to claim 1, characterized by the fact that the weight of the sugars in the pre-impregnated liquid stream, in relation to the weight of the lignocellulosic biomass sugars in the feed stream, is less than 5% by weight.
    [0003]
    3. Process, according to claim 1, characterized by the fact that the pre-impregnation is done in a period of time less than 48 hours.
    [0004]
    4. Process according to claim 1, characterized by the fact that the impregnated liquid stream is filtered through a nanofiltration procedure.
    [0005]
    5. Process, according to claim 4, characterized by the fact that at least a portion of the impregnated liquid has an instantaneous flow greater than 7 L / h-m2, where the instantaneous flow is a flow that occurs when the volume of 72L of a 190L fraction of at least a portion of the impregnated liquid has passed through a spiral nanofilter membrane, where the specification of the membrane is a type of polyamide thin film composed of polyester, presenting a rejection of magnesium sulfate greater than or equal to 98%, when measured in 2000 ppm of magnesium sulfate in water, at a pressure of 9 bar and temperature of 25 ° C, and having an external diameter of 64.0 to 65.0 mm, a length of 432 mm and an internal diameter of 21 mm, the membrane having a cross flow of 1.3-1.8 m3 / h, with a maximum pressure drop of 0.6 bar, in viscosity of 1 cP, and an area of 0.7 m2 membrane model.
    [0006]
    Process according to claim 1, characterized in that said at least a portion of the impregnated liquid of the second impregnated biomass to create an impregnated liquid stream still contains one or more of the substances monomeric sugar, oligomeric sugars, acetic acid and furfural, and that the process further comprises the following steps: E) separating at least a portion of the impregnated liquid from the suspended solids from the impregnated liquid stream comprising monomeric sugars, oligomeric sugars, acetic and furfural acid; and F) filtering at least a portion of the acetic acid from at least a portion of the impregnated liquid, in order to create a permeate and a retentate.
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    同族专利:
    公开号 | 公开日
    AU2012360035A1|2014-08-21|
    CA2859495A1|2013-07-04|
    EP2610346A1|2013-07-03|
    PH12014501510A1|2014-10-08|
    PE20141950A1|2014-12-20|
    ITTO20111219A1|2013-06-29|
    CU20140077A7|2014-12-26|
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    RU2014125902A|2016-02-20|
    EP2798073A1|2014-11-05|
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    CO7101227A2|2014-10-31|
    JP2015506171A|2015-03-02|
    EP2798073B1|2017-07-26|
    WO2013098789A1|2013-07-04|
    EP2610346B1|2014-07-30|
    AU2012360035B2|2016-02-25|
    SG11201403549PA|2014-07-30|
    DK2610346T3|2014-11-03|
    CL2014001746A1|2014-11-21|
    MX2014008000A|2015-02-10|
    ES2518218T3|2014-11-04|
    TN2014000260A1|2015-09-30|
    CN104169429A|2014-11-26|
    CN104169429B|2016-11-16|
    PL2798073T4|2018-01-31|
    KR20140127223A|2014-11-03|
    PL2610346T3|2015-02-27|
    BR112014016039A8|2017-07-04|
    ZA201404686B|2015-12-23|
    HRP20171557T1|2018-02-09|
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    法律状态:
    2018-03-27| B06F| Objections, documents and/or translations needed after an examination request according art. 34 industrial property law|
    2019-12-03| B06U| Preliminary requirement: requests with searches performed by other patent offices: suspension of the patent application procedure|
    2020-04-07| B06A| Notification to applicant to reply to the report for non-patentability or inadequacy of the application according art. 36 industrial patent law|
    2020-08-04| B09A| Decision: intention to grant|
    2020-11-17| B16A| Patent or certificate of addition of invention granted|Free format text: PRAZO DE VALIDADE: 20 (VINTE) ANOS CONTADOS A PARTIR DE 28/12/2012, OBSERVADAS AS CONDICOES LEGAIS. |
    优先权:
    申请号 | 申请日 | 专利标题
    ITTO2011A001219|2011-12-28|
    IT001219A|ITTO20111219A1|2011-12-28|2011-12-28|IMPROVED PRE-IMPREGNATION PROCEDURE FOR BIOMASS CONVERSION|
    PCT/IB2012/057790|WO2013098789A1|2011-12-28|2012-12-28|Improved pre-soaking process for biomass conversion|
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