Method for increasing the throughput and/or reducing the energy usage of a pulping process
阅读说明：本技术 提高制浆工艺的吞吐量和/或降低能量使用的方法 (Method for increasing the throughput and/or reducing the energy usage of a pulping process ) 是由 J·A·兰多尔夫 L·J·里斯 F·莱费尔德 A·费森贝克尔 于 2018-06-12 设计创作，主要内容包括：本发明涉及提高制浆工艺的吞吐量和/或降低能量使用的方法,包括如下步骤：提供多量木质纤维素屑、提供精炼组合物、向多量木质纤维素屑施加精炼组合物和机械精炼多量木质纤维素屑以形成纸浆。精炼组合物包括水和包含糖和醇的反应产物的润滑添加剂。向木质纤维素屑施加精炼组合物的步骤在机械精炼木屑以形成纸浆的步骤前少于5分钟或同时进行。(The invention relates to a method for increasing the throughput and/or reducing the energy usage of a pulping process, comprising the steps of: providing a plurality of lignocellulosic chips, providing a refining composition, applying the refining composition to the plurality of lignocellulosic chips, and mechanically refining the plurality of lignocellulosic chips to form a pulp. The refining composition includes water and a lubricity additive comprising a reaction product of a sugar and an alcohol. The step of applying the refining composition to the lignocellulosic chips is performed less than 5 minutes or simultaneously prior to the step of mechanically refining the chips to form the pulp.)
1. A method of increasing the throughput and/or reducing the energy usage of a pulping process, the method comprising the steps of:
A. providing a plurality of lignocellulosic chips;
B. providing a refining composition comprising:
(i) water, and
(ii) a lubricious additive present in an amount of from 0.01 to 10 wt.%, based on the total weight of the multi-amount lignocellulosic chips, the lubricious additive comprising a reaction product of a sugar and an alcohol;
C. applying a refining composition to the high amount of lignocellulosic chips; and
D. mechanically refining a quantity of lignocellulosic chips to form a pulp;
wherein the step of applying the refining composition to the lignocellulosic chips is performed less than 5 minutes or simultaneously prior to the step of mechanically refining the chips to form the pulp.
2. A method as claimed in claim 1 wherein the sugar has the formula: [ C ]6H12O6]n+1Wherein n is the average of 0, 1,2, 3, 4, 5, 6, 7 or 8.
3. The process of claim 1 or 2, wherein the alkyl alcohol has the formula: ROH, wherein R is an alkyl group having 1to 20 carbon atoms.
4. The method of any one of the preceding claims, wherein alkyl alcohol is further defined as comprising a fatty acid having the formula: a first alkyl alcohol of ROH, wherein R is an alkyl group having 1to 20 carbon atoms, and having the formula: a second alkyl alcohol different from the first alkyl alcohol of R 'OH, wherein R' is independently an alkyl group having 1to 20 carbon atoms.
5. The method of any of the preceding claims, wherein the lubricious additive has the following general structure:
wherein n is an average value and greater than 0 and each R is an alkyl group having 2 to 19 carbon atoms.
6. A method as claimed in any one of the preceding claims, wherein the average value of n +1 is the degree of polymerisation of the lubricity additive and is from 1.2 to 2.5.
7. The method of any one of the preceding claims, wherein R is an alkyl group having from 8 to 14 carbon atoms.
8. A process as claimed in any one of the preceding claims wherein the lubricity additive is present in the refining composition in an amount of from 0.2 to 10% by weight based on the total weight of the macrolignocellulosic chip.
9. The process of any of the preceding claims, wherein water is present in the refining composition in an amount of from 50 to 99.5 wt.%, based on the total weight of the refining composition.
10. The method of any one of the preceding claims, wherein the refining composition has a pH of 6 to 8.
11. The method of any of the preceding claims, wherein the refining composition consists essentially of the lubricious additive and water.
12. A method according to any one of the preceding claims, wherein the step of applying a refining composition to the high amount of lignocellulosic chips is performed not more than 4 minutes before the step of mechanically refining the chips to form the pulp.
13. A method according to any one of the preceding claims, wherein the step of applying a refining composition to the high amount of lignocellulosic chips is performed simultaneously with the step of mechanically refining the chips to form the pulp.
14. A method according to any one of the preceding claims wherein the step of mechanically refining the multivolume of lignocellulosic chips to form the pulp comprises the step of mechanically refining the multivolume of lignocellulosic chips in a primary refiner and then further mechanically refining the multivolume of lignocellulosic chips in a secondary refiner.
15. A method as set forth in claim 12 wherein 25 to 100% by weight of the total amount of refining composition applied to the macroligno-cellulosic chips during the step of mechanically refining the macroligno-cellulosic chips is applied in the primary refiner.
16. A method as set forth in claim 12 or 13 wherein the step of mechanically refining the multivolume of lignocellulosic chips to form the pulp comprises the steps of mechanically refining the multivolume of lignocellulosic chips in a primary refiner, further mechanically refining the multivolume of lignocellulosic chips in a secondary refiner, and re-mechanically refining the multivolume of lignocellulosic chips in a tertiary refiner.
17. A method as set forth in claim 14 wherein the step of applying the refining composition to the multivolume of lignocellulosic chips is further defined as applying all or a portion of the refining composition directly to the multivolume of lignocellulosic chips in the primary, secondary, and/or tertiary refiners.
18. A process according to any one of the preceding claims wherein the refining composition has a temperature of from 5 to 99 ℃ when applied to the macroligno-cellulosic chips.
19. The method according to any one of the preceding claims, wherein the step of mechanically refining the macrolignocellulosic chips to form a pulp is performed at a rate of 1kg/hr to 100 ton/hr.
20. The method of any one of the preceding claims, wherein the amount of energy used during the refining step is at least 5% less than the reference amount of energy used during the refining step of the reference method that does not utilize the claimed lubricity additive.
21. The method of any one of the preceding claims, having a throughput that is at least 1% higher than the reference throughput of a reference method that does not utilize the claimed lubricity additive, and the amount of energy used during the refining step is equal to or less than the reference amount of energy used during the refining step of the reference method that does not utilize the claimed lubricity additive.
22. The method of any preceding claim, wherein the pulp has a Canadian Standard Freeness (CSF) of from 50 to 800 when tested in accordance with TAPPI T227 and/or a wet tensile strength of from 100to 8,000N/m when tested in accordance with TAPPI 494.
Description of the related Art
As is known in the pulping industry, lignocellulosic material, such as wood chips, is chemically and/or mechanically refined in various pulping processes to be pulped. Lignocellulosic material used for pulping comprises four main components, cellulose fibers, lignin (a three-dimensional polymer that binds cellulose fibers together), hemicellulose (a shorter branched carbohydrate polymer) and water. The pulping process separates the cellulose fibers within the lignocellulosic material, and the separated cellulose fibers are referred to as pulp. Chemical pulping processes utilize various caustic chemicals to break down lignin and hemicellulose and separate cellulose fibers within lignocellulosic materials to form pulp. Mechanical pulping processes mechanically refine, i.e., physically tear, the cellulose fibers within the lignocellulosic material to form a pulp comprising separated cellulose fibers.
The pulp mill utilizes various mechanical pulping processes known in the pulping industry including Stone Groundwood (SGW), Pressure Groundwood (PGW), Refiner Mechanical Pulp (RMP), pressurized RMP (prmp), heated RMP (trmp), thermomechanical pulp (TMP), thermochemical pulp (TCMP), thermomechanical chemical pulp (TMCP), long fiber chemimechanical pulp (LFCMP), and Chemically Treated Long Fibers (CTLF) to produce pulp on a pulp production line. Many modern pulp mills utilize capital-intensive continuous pulp production lines that mechanically refine wood chips by grinding between ridged metal discs known as refiner plates. The throughput of the pulp line is limited and the mechanical pulping process requires a considerable amount of energy. There remains an opportunity to develop an improved mechanical pulping process.
Summary of the disclosure and advantages
The method of the present disclosure increases the throughput of the pulping process and/or reduces energy usage and comprises the steps of: providing a plurality of lignocellulosic chips, providing a refining composition, applying the refining composition to the plurality of lignocellulosic chips, and mechanically refining the plurality of lignocellulosic chips to form a pulp. The refining composition includes water and a lubricity additive comprising a reaction product of a sugar and an alcohol. The step of applying the refining composition to the lignocellulosic chips is performed less than 5 minutes or simultaneously prior to the step of mechanically refining the chips to form the pulp. Advantageously, the process is efficient in producing pulp having desirable chemical and physical properties, such as strength, brightness, opacity, freeness, and the like.
Brief description of several views of the drawings
Other advantages of the present disclosure will be readily appreciated, as the same becomes better understood by reference to the following detailed description when considered in connection with the accompanying drawings wherein:
fig. 1 is a flow diagram depicting various embodiments of the methods of the present disclosure for increasing the throughput and/or reducing energy usage of a pulping process.
Fig. 2 is a bar graph showing water absorption of high amounts of lignocellulosic chips to which the lubricating composition of the present disclosure is applied.
Detailed description of the disclosure
The present disclosure provides a method of increasing the throughput and/or reducing energy usage of a pulping process. As described in detail herein, the method comprises the steps of: providing a plurality of lignocellulosic chips, providing a refining composition, applying the refining composition to the plurality of lignocellulosic chips, and mechanically refining the plurality of lignocellulosic chips to form a pulp. The methods of the present disclosure may be used in any mechanical pulping process known in the art. The present process may include one or more of these process steps associated with the separation and recovery of cellulose, but these steps are not essential.
The term "lignocellulosic chip" is used to describe a chip of lignocellulosic material. Lignocellulosic material is not particularly limited and can be further defined as being, or comprising, consisting essentially of (e.g., free of non-lignocellulosic material), or consisting of material (or precursors thereof) derived from wood, bagasse, straw, flax residue, nut shells, grain hulls, or any material comprising lignin and cellulose, and combinations thereof. In various embodiments, lignocellulosic materials are prepared from various species of hardwoods and/or softwoods, as understood in the art. Lignocellulosic materials can be derived from a variety of processes, such as by pulverizing logs, industrial wood waste, strands, raw wood pulp, and the like into chips in the form of chips, flakes, chips, slivers, scrims (scrims), fibers, sheets, and the like. Most commonly, lignocellulosic materials are further defined as lignocellulosic chips, wood chips, or wood pulp.
Refining the composition:
the refining composition includes a lubricity additive comprising the reaction product of a sugar and an alcohol and water.
I.Lubricating additive:
the lubricious additive is made by reacting a monosaccharide or a compound that is hydrolysable to a monosaccharide with an alcohol, such as a fatty alcohol, in an acid medium.
The sugar has the formula: [ C ]6H12O6]n+1Wherein n is an average value of 0 or more. In various embodiments, n is an average value of 0, 1,2, 3, 4, 5, 6, 7, or 8. In various embodiments, n is an average value of 0to 8, 1to 7, 1to 3, 1to 2, 2 to 6, 3 to 5, or 4 to 5. In various embodiments, n +1 has a value of 1to 3, 1to 2.5, 1to 2, 1.5 to 3, 1.5 to 2.5, 1.5 to 2, 1.2 to 2.5, 1.1 to 1.9, 1.2 to 1.8, 1.3 to 1.7, 1.4 to 1.6, 1.4 to 1.8, or 1.5. In other embodiments, n +1 is an average of 1.1, 1.2, 1.3, 1.4, 1.5, 1.6, 1.7, 1.8, 1.9, or 2.
Any sugar having the above formula or any isomer thereof may be used. For example, the sugar may be an aldohexose or a ketohexose. In various embodiments, the saccharide is selected from the group consisting of allose, altrose, galactose, glucose, gulose, idose, mannose, talose, and combinations thereof. In other embodiments, the sugar is selected from the group consisting of fructose, psicose, sorbose, tagatose, and combinations thereof. In a further embodiment, the sugar is selected from the group consisting of glucose, fructose and galactose. In a further embodimentThe sugar is glucose or fructose or galactose. The saccharides may each be of formula C6H12O6Any one or more of the above sugars. Further, when n is greater than 0, the saccharide can be any one or more complexes of the above saccharides. These complexes may also be described as carbohydrates.
Typically, the lubricious additive is formed from, i.e., includes, as its structural unit, glucose. It is contemplated that any known isomer or anomer of glucose may be used. For example, glucose has four optical centers, so that glucose can have 15 optical stereoisomers, any of which can be used.
The alkyl alcohol has the formula: ROH, wherein R is an alkyl group having 1to 20 carbon atoms. The alkyl group can have any number of carbon atoms from
In a particular embodiment, the alkyl alcohol is further defined as comprising a compound having the formula: a first alkyl alcohol of ROH, wherein R is an alkyl group having 1to 20 carbon atoms, and having the formula: a second, different alkyl alcohol of R 'OH, wherein R' is independently an alkyl group having 1to 20 carbon atoms. R and R' may each be any of the values described above. In various embodiments, R and/or R' are independently 8, 10, 12, 14, or 16. In other embodiments, R and/or R' are each independently 9, 11, 13, 15, or 17. Moreover, all values and ranges of values inclusive of and between the above values are expressly contemplated herein for use in a non-limiting embodiment.
Combining an alkyl alcohol and a sugar to form a compound having the formula [ C6H12O6][C6H11O5]nOR a lubricity additive. Each moiety of the formula may be C6H12O6Any isomer of (a). In other words, C may be used in any part of the above formula6H12O6Any structure or form of (a). First of the above formula [ C6H12O6]May be related to the second [ C ]6H12O6]Different isomers. In various additional non-limiting embodiments, all numbers and ranges of numbers between and including the numbers recited above are hereby expressly contemplated.
Further, R may be any alkyl
In various embodiments, the lubricious additive may be generally described as having the structure:
wherein n is as described above.
In other embodiments, n is 1 or greater. In various embodiments, the average value of n +1 is the degree of polymerization of the lubricious additive and is 1.2 to 2.5, 1.3 to 1.7, or 1.5 to 1.7. In various embodiments, the average value of n +1 is 1.2, 1.3, 1.4, 1.5, 1.6, 1.7, 1.8, 1.9, 2, 2.1, 2.2, 2.3, 2.4, or 2.5. In various additional non-limiting embodiments, all numbers and ranges of numbers between and including the numbers recited above are expressly contemplated herein.
In a further embodiment, the lubricious additive has the structure:
wherein R may be any of those described above, for example C8-C14 or any in between.
Suitable examples of commercially available lubricious additives include, but are not limited to, those available from BASF corp
From a compatibility standpoint, the lubricant additive is soluble in alkaline, sulfite, and certain acidic solutions. Thus, the refinery composition may use the lubricious additive with a wide range of other components.
In addition, the lubricant additive is resistant to electrolytes in solution, such as sodium hydroxide and sodium sulfite. Thus, the refinery composition comprising the lubricity additive is particularly stable and effective in the presence of electrolytes.
The lubricant additive rapidly wets through the lignocellulosic chips during the mechanical pulping process and effectively reduces the energy consumption required to refine the lignocellulosic chips without adversely affecting the products formed from the finished pulp. More specifically, the lubricious additive does not affect the critical properties of the pulp and products formed therefrom.
In various embodiments, the lubricity additive is present in the refining composition in an amount of less than 10, 9, 8, 7, 6, 5, 4, 3, 2, 1, 0.5, 0.4, 0.3, 0.2 weight percent based on the total weight of the macrolignocellulosic chip. In other embodiments, the lubricious additive is present in an amount of from 0.01 to 10, from 0.2 to 10, from 0.5 to 8, or from
II.Water:
the refining composition also includes water. The type or purity of water is not particularly limited and may include distilled water, well water, tap water, and the like. Furthermore, the amount of water present in the refining composition is also not particularly limited. In various embodiments, water is present in the refining composition in an amount of greater than 5, 10, 15, 20, 25, 30, 35, 40, 45, 50, 55, 60, 65, 70, 75, 80, 85, 90, 91, 92, 93, 94, 95, 96, 97, 98, or 99 weight percent based on the total weight of the refining composition. In other embodiments, the water is present in an amount of 50 to 99.5, 80 to 99.5, 90 to 99, or 95 to 99 weight percent based on the total weight of the refining composition. It is contemplated that one or more of the above-described values can be any value or range of values (whole and fractional) within the above-described ranges and/or can vary by 5%, ± 10%, ± 15%, ± 20%, ± 25%, ± 30%, etc.
III.Addition of additives:
in addition to the lubricity additive and water, the refinery composition may also include one or more additional additives including, but not limited to, corrosion inhibitors, surfactants, pH adjusters, thickeners, stabilizers, odorants, colorants, and combinations thereof. Additives, if included, may be included in the composition in various amounts. In some embodiments, the additives included may be nonionic, anionic, or cationic.
In some embodiments, the refining composition may include a corrosion inhibitor. Corrosion inhibitors may be generally defined as substances that, when added, reduce the corrosion rate of the metal of various materials exposed to the ethanol process. For this reason, corrosion inhibitors may be used to inhibit corrosion of the surfaces of equipment used in the process. The process may include any corrosion inhibitor known in the art. Of course, the refining composition may comprise more than one corrosion inhibitor, i.e. a combination of different corrosion inhibitors. In one embodiment, the corrosion inhibitor includes an amphoteric surfactant. Thus, the corrosion inhibitor may be an amphoteric surfactant or may include one or more additional components, such as water. If the corrosion inhibitor includes water, the amphoteric surfactant can be provided in various concentrations. For the purposes of this disclosure, suitable amphoteric surfactants include betaines, imidazolines, and propionates. Further examples of suitable amphoteric surfactants include sulfobetaines, amphopropionates, amphodipropionates, aminopropionates, aminodipropionates, amphoacetates, amphodiacetates, and amphohydroxypropylsulfonates. In certain embodiments, the amphoteric surfactant is at least one of a propionate or an amphodiacetate. Further specific examples of suitable amphoteric surfactants include N-acyl amino acids, such as N-alkyl aminoacetate and disodium cocoamphodiacetate, and amine oxides, such as stearyl amine oxide. In one embodiment, the amphoteric surfactant comprises disodium cocoamphodiacetate.
In some embodiments, the refining composition may include a surfactant. The surfactant is typically selected from the group consisting of nonionic surfactants, anionic surfactants, and ionic surfactants. For purposes of this disclosure, suitable amphoteric surfactants include polyalkylene oxides, alkyl polyalkylene oxides, polyoxyethylene sorbitan monolaurate, alkyl polyglucosides, anionic derivatives of alkyl polyglucosides, fatty alcohols, anionic derivatives of fatty alcohols, and phosphate esters.
However, in other embodiments, the refining composition consists of, or consists essentially of, a lubricious additive and water. Embodiments of the refining composition consisting essentially of the lubricious additive and water are free of any additional additives or other components that would materially affect the basic and novel characteristics of the claimed invention.
In some embodiments, the composition is free of additives including, but not limited to, surfactants, corrosion inhibitors, chelating agents, polymers, acrylic polymers, acids, bases, alcohols, and/or polyols. In other embodiments, the refining composition is free of surfactants, corrosion inhibitors, chelating agents, polymers, acrylic polymers, acids, bases, alcohols, and/or polyols. The term "free" as used herein with respect to a component that may be included in a refining composition can be defined as including less than 0.5 or less than 0.1 or less than 0.01 or including 0 wt% of the component based on the total weight of the refining composition.
IV.Properties of the refining composition:
the refining composition is effective at neutral pH and is therefore not caustic in nature. In many embodiments, the refining composition has a pH of 1.5 to 12, 4 to 10, 5 to 9, 6 to 8, or 6.5 to 7.5. All values and ranges of values between the above-mentioned values are hereby expressly contemplated in various non-limiting embodiments.
In some embodiments, the refining composition has a Draves wetting time of less than 100 seconds as determined using ASTM D2281. In various embodiments, the refining composition has a delaves wetting time of less than 95, 90, 85, 80, 75, 70, 65, 60, 55, 50, 45, 40, 35, 30, 25, 20, 15, 10, or 5 seconds, as determined using ASTM D2281, or any range thereof, including any and all fractional values and ranges of fractional values within those described above. In other embodiments, the refining composition has a delaves wetting time of
The method comprises the following steps:
the methods of the present disclosure increase the throughput of the pulping process and/or reduce energy usage. In the pulping process, lignocellulosic chips are mechanically refined to pulp. Lignocellulosic chip comprises four major components, cellulose fibers, lignin (a three-dimensional polymer that binds cellulose fibers together), hemicellulose (a shorter branched carbohydrate polymer), and water. The pulping process refines, i.e., physically tears, the cellulose fibers within the lignocellulosic chips to form a pulp that includes separated cellulose fibers.
As described above, the method of the present disclosure includes the step of providing lignocellulosic chips. The providing step is not particularly limited and may include conveying, supplying, and the like. In various embodiments, the providing step may be further defined as supplying the lignocellulosic chips in one or more forms as described above by grinding, shredding, and cutting the lignocellulosic material or precursors thereof. In one embodiment, the lignocellulosic material comprises, consists essentially of, or consists of lignocellulosic chips, such as wood chips.
The method of the present disclosure further comprises the step of providing a refining composition. The refining composition is as described immediately above. The providing step is not particularly limited and may include conveying, supplying, and the like. In various embodiments, the providing step can be further defined as supplying the refining composition in one or more forms, for example as a concentrate to be diluted.
In some embodiments, the lubricious additive is provided in pure form and then diluted with a solvent, such as water, prior to the step of applying the refining composition to the lignocellulosic chips to form the lubricious composition.
It is also contemplated herein that the refining composition may be supplied as two or more separate components that may be blended together prior to use. For example, the refinery composition may be supplied in a two component system, one component containing the lubricity additive and the other component containing water and other additives. In this example, the two components may be provided separately and blended together on site immediately prior to use and, if desired, diluted with water at the point of use.
The method of the present disclosure includes the step of applying a refining composition to the high amount of lignocellulosic chips. In some embodiments, the refining composition is applied to the multivolume lignocellulosic chips at a temperature of 5 to 99, 5 to 85, 5 to 45, or 15 to 35 ℃. All values and ranges of values between the above-mentioned values are hereby expressly contemplated in various non-limiting embodiments.
Applying a refining composition to the amount of lignocellulosic chips. In some embodiments, the refining composition is applied in an amount of from 0.5 to 125, from 5 to 100, or from 10 to 80 weight percent based on the total weight of the multivolume lignocellulosic chip. Alternatively, the refining composition is applied in an amount such that the lubricity additive is present in an amount of 0.01 to 10, 0.01 to 5, 0.01 to 2.0, 0.01 to 1.0, 0.1 to 0.7, or 0.1 to 0.5 weight percent based on the total weight of the refined multi-amount lignocellulosic chips. All values and ranges of values between the above-mentioned values are hereby expressly contemplated in various non-limiting embodiments.
The method of the present disclosure includes the step of mechanically refining the plurality of lignocellulosic chips to form a pulp. During the step of mechanically refining the mass of lignocellulosic chips, the cellulosic fibers within the lignocellulosic chips are torn to form a pulp comprising separated cellulosic fibers. In a typical embodiment, the step of mechanically refining the mass of lignocellulosic chips is performed in a refiner, which mechanically refines the cellulosic chips by grinding between ridge-shaped metal discs, known as refiner plates.
In various embodiments, the step of mechanically refining the plurality of lignocellulosic chips to form a pulp is performed in one or more refiners, such as any combination of primary, secondary, and tertiary refiners. In one example, an embodiment of the method includes a single step of mechanically refining the plurality of lignocellulosic chips in a refiner to form a pulp. In another embodiment, an embodiment of the method includes the step of mechanically refining the mass of lignocellulosic chips in a primary refiner and then further mechanically refining the mass of lignocellulosic chips in a secondary refiner. In yet another example, an embodiment of the method includes the steps of mechanically refining the plurality of lignocellulosic chips in a primary refiner, further mechanically refining the plurality of lignocellulosic chips in a secondary refiner, and mechanically refining the plurality of lignocellulosic chips in a tertiary refiner. Figure 1 is a flow diagram depicting various embodiments of the methods of the present disclosure for increasing the throughput and/or reducing energy usage of a pulping process utilizing primary, secondary and tertiary refiners.
The refining composition increases throughput and/or reduces energy usage during the step of mechanically refining the amount of lignocellulosic chips to form pulp. Advantageously, there is no need to saturate the lignocellulosic chips in the refining composition. The refining composition reduces the energy required during refining and has a very short residence time on the lignocellulosic chips. To this end, in the method of the present disclosure, the step of applying the refining composition to the lignocellulosic chips is performed less than 5 minutes or simultaneously prior to the step of mechanically refining the chips to form the pulp. In some embodiments, the step of applying a refining composition to the high amount of lignocellulosic chips is performed no more than 4, no more than 3, no more than 2, and no more than 1 minute prior to the step of mechanically refining the chips to form the pulp.
In many embodiments, the step of applying a refining composition to the mass of lignocellulosic chips is performed simultaneously with the step of mechanically refining the chips to form the pulp.
In many embodiments, the step of applying a refining composition to the plurality of lignocellulosic chips comprises one or more substeps, or one or more applications of a refining composition. For example, in one embodiment of the method, 5 to 100, or 25 to 100 wt% of the total amount of refining composition is applied to the multivolume lignocellulosic chips in the primary refiner during the step of mechanically refining the multivolume lignocellulosic chips. In some embodiments, all or a portion of the refining composition is applied to the plurality of lignocellulosic pieces in the primary, secondary and/or tertiary refiner. All values and value ranges between the above-mentioned values, such as the fraction of refining composition applied in the primary, secondary and tertiary refiners, are expressly contemplated herein in various non-limiting embodiments.
In some embodiments, the method is further defined as a continuous process, wherein the step of mechanically refining the multivolume lignocellulosic chips to form a pulp is performed at a rate of 1kg/hr to 1000ton/hr, 50kg/hr to 700ton/hr, 500kg/hr to 500ton/hr, or 1ton/hr to 300 ton/hr. All values and ranges of values between the above-mentioned values are hereby expressly contemplated in various non-limiting embodiments.
In many embodiments of the method, the amount of energy used during the refining step is at least 5, at least 6, at least 7, at least 8, at least 9, at least 10, at least 11, at least 12, at least 13, at least 14, at least 15, at least 16, at least 17, at least 18, at least 19, at least 20, at least 25, at least 30, at least 35, at least 40, at least 45% less than the reference amount of energy used during the refining step of a reference method that does not utilize the claimed lubricity additive. Alternatively, in some embodiments of the method, the amount of energy used during the refining step is 1to 50, 5 to 40, 5 to 30, 5 to 20, 10 to 20, or 8 to 16% less than the reference amount of energy used during the refining step of a reference method that does not utilize the claimed lubricity additive during the refining step.
In many embodiments of the method, the amount of energy used during the refining step is at least 5, at least 6, at least 7, at least 8, at least 9, at least 10, at least 11, at least 12, at least 13, at least 14, at least 15, at least 16, at least 17, at least 18, at least 19, at least 20, at least 25, at least 30, at least 35, at least 40, or at least 45% less than the reference amount of energy used during the refining step of a reference method that does not utilize any surfactants or lubricity additives. Alternatively, in some embodiments of the method, the amount of energy used during the refining step is 1to 50, 5 to 40, 5 to 30, 5 to 20, 10 to 20, or 8 to 16% less than the reference amount of energy used during the refining step of a reference method that does not utilize any surfactant or lubricious additive during the refining step.
In many embodiments of the method, the throughput is at least 1, at least 5, at least 6, at least 7, at least 8, at least 9, at least 10, at least 11, at least 12, at least 13, at least 14, at least 15, at least 16, at least 17, at least 18, at least 19, or at least 20% higher than the reference throughput of a reference method that does not utilize the claimed lubricity additive when the amount of energy used during the refining step is equal to or less than the reference amount of energy used during the refining step of the reference method that does not utilize the claimed lubricity additive during the refining step. Alternatively, in some embodiments of the method, when the amount of energy used during the refining step is equal to or less than the reference amount of energy used during the refining step of the reference method that does not utilize the claimed lubricity additive during the refining step, the throughput is 1to 20, 5 to 20, 10 to 20, or 8 to 16% higher than the reference throughput of the reference method that does not utilize the claimed lubricity additive.
In many embodiments of the method, the throughput is at least 1, at least 5, at least 6, at least 7, at least 8, at least 9, at least 10, at least 11, at least 12, at least 13, at least 14, at least 15, at least 16, at least 17, at least 18, at least 19, or at least 20% higher than the reference throughput of a reference method that does not utilize a surfactant or a lubricity additive when the amount of energy used during the refining step is equal to or less than the reference amount of energy used during the refining step of the reference method that does not utilize any surfactant or lubricity additive during the refining step. Alternatively, in some embodiments of the method, when the amount of energy used during the refining step is equal to or less than the reference amount of energy used during the refining step of a reference method that does not utilize any surfactant or claimed lubricity additive during the refining step, the throughput is 1to 20, 5 to 20, 10 to 20, or 8 to 16% higher than the reference throughput of the reference method that does not utilize any surfactant or lubricity additive.
As mentioned above, pulp mills utilize mechanical pulping processes, which are problematically energy intensive. Therefore, there is a need for solutions, such as the present method, that increase the throughput of mechanical pulping without increasing the energy usage, or that decrease the energy usage of such mechanical pulping processes at standard throughput. Of course, such a solution should not impair the pulp quality. Without being bound by theory, it is believed that the lubricity additive reduces the surface tension of the water of the refining composition and enables the water to better penetrate the high amount of lignocellulosic chips to bring about a higher water uptake, which "swells" and softens the high amount of lignocellulosic chips to enable a reduction in refining energy, which does not affect the pulp quality (or the quality of the paper formed from the pulp).
In many embodiments of the method, the pulp made with the method of the present disclosure has a degree of fibrillation as measured according to Canadian Standard Freeness ("CSF") of 50 to 800, 75 to 600, or 100to 300. Alternatively, the CSF of the pulp made with the method of the present disclosure is about ± 5, about ± 10, about ± 15, about ± 20, about ± 25% of the degree of fibrillation of the pulp made by the reference method without the claimed lubricity additive. In additional non-limiting embodiments, all numbers and ranges that are within the endpoints of the ranges noted above and that include the endpoints are hereby expressly contemplated.
CSF is an empirical test procedure for measuring the drainage rate of 3 grams of fibrous pulp material in 1 liter of water. CSF measurements were performed according to TAPPI T227 test procedure. In making CSF measurements, it is noted that a more fibrillated fibrous pulp material has a lower drainage rate and thus a lower "ml CSF" value, and that a less fibrillated fibrous pulp material has a higher "ml CSF" value.
In many embodiments of the method, the pulp made with the method of the present disclosure has a wet tensile strength of 100to 8,000, 600 to 6,000, or 1,200 to 4,000N/m when tested according to TAPPI T494.
The following examples, which illustrate the compositions and methods of the present disclosure, are intended to illustrate and not to limit the present disclosure.
Examples
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