阅读说明：本技术 一种秸秆零排放制浆和生产木素新工艺 (Straw zero-discharge pulping and lignin production novel process ) 是由 曲香华 于 2019-06-13 设计创作，主要内容包括：本发明公开了一种秸秆零排放制浆和生产木素新工艺,属于制浆造纸领域。一种秸秆零排放制浆和生产木素新工艺,其制备工艺如下：步骤一：备料,收集所需的农业秸秆；步骤二：预处理,将农业秸秆进行碎草除尘后,精料送入预浸设备内,在常压和一定温度范围内,将上次蒸煮制浆的废水加入预处理设备再次使用,将上次低温制浆的黑液完全置入预处理罐中,同时补充部分清水,混合热予浸；本发明提供一种在低温常压条件下,制浆水零排放,提取的木质素分子量分布的均一化程度高,制得质量稳定草浆的零排放制浆工艺,可大规模利用废弃的秸秆等可再生资源造纸,节能环保,并且变废为宝,具有良好的社会效益和经济效益。(The invention discloses a new process for straw zero-emission pulping and lignin production, belonging to the field of pulping and papermaking. A new process for pulping and producing lignin with zero discharge of straws comprises the following steps: the method comprises the following steps: preparing materials, and collecting needed agricultural straws; step two: pre-treating, namely, after grass crushing and dust removal are carried out on agricultural straws, fine materials are sent into pre-soaking equipment, the waste water obtained by the last cooking pulping is added into the pre-treating equipment for reuse at normal pressure and within a certain temperature range, the black liquor obtained by the last low-temperature pulping is completely put into a pre-treating tank, meanwhile, partial clear water is supplemented, and the pre-soaking is carried out by mixing heat; the zero-emission pulping process for preparing the straw pulp has the advantages that under the conditions of low temperature and normal pressure, zero emission of pulping water is realized, the uniformity degree of the molecular weight distribution of the extracted lignin is high, the straw pulp with stable quality is prepared, the waste straws and other renewable resources can be utilized for papermaking in a large scale, the energy is saved, the environment is protected, the waste is changed into the valuable, and the social benefit and the economic benefit are good.)

1. A new process for straw zero-emission pulping and lignin production is characterized in that the preparation process comprises the following steps:

the method comprises the following steps: preparing materials and collecting the needed agricultural straws.

Step two: pre-treating, namely, after grass crushing and dust removal are carried out on agricultural straws, fine materials are sent into pre-soaking equipment, the waste water obtained by the last cooking pulping is added into the pre-treating equipment for reuse at normal pressure and within a certain temperature range, the black liquor obtained by the last pulping at normal temperature is completely put into a pre-treating tank, meanwhile, partial clear water is supplemented, the mixture is heated for pre-soaking, and after a period of time, the pulp A1 and the black liquor B1 are separated by extrusion of a pulp extruder a.

Step three: cooking, namely putting the slurry A1 into a high-concentration hydraulic pulper, adding a high-concentration solution c1, and reacting at the temperature of 90-100 ℃ for 60-90 minutes; under the condition of a certain pH value, adding highly concentrated solution c2, keeping the temperature at 90-100 ℃, continuing to react for 30-60 minutes, and extruding and separating pulp A2 and black liquor B2 by a pulp extruder B.

Step four: and (3) precipitating in an inclined tube, allowing the black liquor B1 to enter the inclined tube for precipitation to complete solid-liquid separation, allowing the lower-layer solid C to pass through a filter cake of a plate-and-frame filter press and be sent to a boiler for combustion treatment, and returning the liquid D to the inclined tube equipment for precipitation again to obtain the supernatant E.

Step five: two-stage DTUF (disc tube ultrafiltration), firstly carrying out primary DTUF (disc tube ultrafiltration) on supernatant E to obtain ultrafiltration concentrated solution F1 and permeate G, wherein the ultrafiltration concentrated solution F1 enters a plate-and-frame filter press, carrying out DTUF (disc tube ultrafiltration) on the permeate G again to obtain ultrafiltration concentrated solution F2 and permeate G, carrying out spray dryer on the ultrafiltration concentrated solution F2 to obtain a lignin product H with the molecular weight of 5000Da to 20000Da, carrying out desalination treatment on the two-time permeate G in DTNF (disc tube nanofiltration), and carrying out re-filtration on the concentrated solution F in the primary DTUF (disc tube ultrafiltration).

Step six: and (3) high-concentration pulping, namely feeding the straw fiber semi-finished pulp with the concentration of 30% into a high-concentration pulping machine, and devillicating and brooming the surface of the straw fiber semi-finished pulp on the basis of keeping the fiber length as much as possible so as to improve the papermaking performance of the straw fiber semi-finished pulp.

Step seven: and (3) pulping, namely, feeding the pulp A into a high-concentration pulping machine for fibrillation to obtain high-quality pulp, and then performing dispatching, deslagging and pressure screening to finally obtain high-quality paper pulp.

2. The new straw zero-emission pulping and lignin production process according to claim 1, wherein the pretreatment solution in the second step comprises the following raw materials in parts by weight: 5-10 parts of NaOH and 2-5 parts of urea.

3. The new straw zero-emission pulping and lignin production process according to claim 1, wherein the weight ratio of the total amount of the black liquor B1 and the clear water to the straw fiber raw material liquor in the second step is 1: 6-10.

4. The new process for straw zero-emission pulping and lignin production according to claim 1, wherein the temperature of the mixed hot pre-soaking in the second step is 80-90 ℃.

5. The novel process for straw zero-emission pulping and lignin production according to claim 1, wherein the pretreatment in the second step is carried out for 30-60 minutes.

6. The new straw zero-emission pulping and lignin production process according to claim 1, wherein the highly concentrated solution c1 of the third step comprises the following raw materials in parts by weight: 5-20 parts of NaOH solution and 8-15 parts of sodium sulfite, wherein the high-concentration solution c2 comprises the following raw materials in parts by weight: 10-20 parts of hydrogen peroxide, 2-5 parts of sodium silicate, 0.2-0.5 part of magnesium sulfate and 0.1-2 parts of metal ion chelating agent.

7. The novel process for straw zero-emission pulping and lignin production according to claim 1, wherein the pH value in the third step is 10, and when the pH value is lower than 10, a small amount of NaOH can be added for adjustment.

8. The novel process for straw zero-emission pulping and lignin production according to claim 1, wherein the permeate liquid G in the fifth step can be recycled.

9. The new straw zero-emission pulping and lignin production process according to claim 1, wherein the retention molecular weight of the primary DTUF (disc tube ultrafiltration) is 20000Da, the retention molecular weight of the secondary DTUF (disc tube ultrafiltration) is 5000Da, and one or more target molecular weight DTUFs (disc tube ultrafiltration) can be inserted between the primary DTUF (disc tube ultrafiltration) and the secondary DTUF (disc tube ultrafiltration) as required.

10. The new straw zero-emission pulping and lignin production process according to claim 1, wherein the black liquor B can be used for the next pretreatment operation.

Technical Field

The invention relates to the technical field of pulping and papermaking, in particular to a novel process for straw zero-emission pulping and lignin production.

Background

The annual yield of crop straws in China is up to 7 hundred million tons, wherein about 4.5 hundred million tons can be collected, but the comprehensive utilization rate is less than 40 percent. The pulping process in a sense is a process of treating lignin and stripping fibers, whether chemical pulping, mechanical pulping or chemi-mechanical, whose main purpose is to break the adhesive force of lignin in the pulping material, because lignin is the most dominant substance existing between intercellular layers, which binds cells to each other and consolidates them. The chemical pulping principle is that chemical substances are added to dissolve out lignin, so that the consolidation among fibers is damaged, but the generated black liquor has high concentration, high viscosity, difficult degradation and serious environmental pollution, and the discharge amount of pollutants accounts for about 90 percent of the discharge amount in the whole papermaking process. The pulping black liquor mainly contains lignin, cellulose and hemicellulose degradation products, pigment, residual alkali and the like, and is a complex pollution source with high alkalinity and high COD. According to incomplete statistics, the pulping black liquor in the papermaking industry in China contains more than 3000 ten thousand tons of lignin, the lignin in the black liquor is reasonably utilized, and the win-win aim of resource utilization of papermaking wastewater and environmental protection can be achieved. The lignin contains a plurality of active groups such as phenolic hydroxyl, carbonyl, alcoholic hydroxyl and the like, and can be used as a precursor of products such as artificial board adhesives, soil conditioners, water treatment agents, water reducing agents, polyurethane and the like. In the alkaline pulping process, lignin in the raw material is fragmented to different degrees under the alkaline action to form alkaline lignin with wider molecular weight distribution range. Differential precipitation, organic solvent precipitation and ultrafiltration technologies can realize the fractional separation of lignin with different molecular weights in the black liquor, wherein the ultrafiltration membrane separation technology has the advantages of good selectivity, no chemical change in the separation process, low energy consumption and the like, and has been applied to the fractional separation of the lignin in the pulping black liquor. However, the pulping black liquor taking bamboo and gramineous plants as raw materials has large viscosity, complex components, large organic matter molecular weight dispersity and poor liquidity, and the application of the ultrafiltration membrane technology in the lignin fractional separation in the black liquor is restricted. At present, the lignin in the black liquor is separated by using an ultrafiltration membrane technology by classification usually by adopting the following auxiliary means: 1. the black liquor can be ultrafiltered only after being diluted to a low solid concentration, and the solid concentration is generally 3-7%; 2. because the attenuation speed of the membrane flux is high, the membrane component needs to be cleaned frequently; 3. the black liquor temperature is increased as much as possible to reduce the black liquor viscosity.

The main problems existing in the utilization of the grass alkali lignin at present are that the lignin has fewer active groups and wider molecular arrangement distribution range, so that the lignin has fewer modified reaction points and high reaction nonuniformity, the content of phenolic hydroxyl groups in the lignin is greatly increased after the lignin is oxidized and oxidized under an alkaline condition, the uniformity of the molecular weight distribution of the lignin is improved, and the reaction points for modification are increased; the phenol content of the product is increased, the molecular weight is reduced, and the homogenization degree of the molecular weight distribution is improved, and the changes are beneficial to improving the surface activity of the oxidized lignin and reducing the surface tension of the aqueous solution of the oxidized lignin. The prevention of physical clogging can be solved by DTUF (disc tube ultrafiltration): the DT component adopts an open flow channel design, the effective flow channel of the feed liquid is wide, and physical blockage is avoided. The minimum scale formation and pollution phenomena adopt the flow guide disc with the convex points for supporting, the feed liquid forms a turbulent flow state in the filtering process, the scale formation, pollution and concentration polarization phenomena on the surface of the membrane are reduced to the maximum extent, the SDI value is allowed to reach 20 high-pollution water source, and the risk of pollution is avoided. Meanwhile, the concentration multiple of DTUF (disc tube ultrafiltration) is high: the operation pressure of the DT module has three grades of 75bar, 150bar and 200bar, and the DT module is a membrane module with the highest pressure grade in the current industrial application, and in some applications with high concentration multiple, the solid content can reach more than 30 percent, and the concentration multiple is high.

With the increase of national environmental protection and the adjustment of rural energy structures, the living utilization rate of the straws is reduced, a large number of paper mills and rice and wheat straw chemical pulping plants are closed, the reutilization rate of the straws is greatly reduced, the waste straws are treated by adopting an incineration mode in rural areas at present, the natural environment is seriously polluted, in order to utilize the straws fully and to the maximum extent, the effective ingredients of the straws need to be separated, and the straws are classified as raw materials for use.

Disclosure of Invention

The invention aims to solve the problems that in the prior art, straw pulping has high energy consumption and low extraction rate in the preparation process, and lignin cannot be extracted and can only be used as waste for biochemical treatment, and provides a novel process for straw zero-emission pulping and lignin production.

In order to achieve the purpose, the invention adopts the following technical scheme:

a new process for pulping and producing lignin with zero discharge of straws comprises the following steps:

the method comprises the following steps: preparing materials and collecting the needed agricultural straws.

Step two: pre-treating, namely, after grass crushing and dust removal are carried out on agricultural straws, fine materials are sent into pre-soaking equipment, the waste water obtained by the last cooking pulping is added into the pre-treating equipment for reuse at normal pressure and within a certain temperature range, the black liquor obtained by the last pulping at normal temperature is completely put into a pre-treating tank, meanwhile, partial clear water is supplemented, the mixture is heated for pre-soaking, and after a period of time, the pulp A1 and the black liquor B1 are separated by extrusion of a pulp extruder a.

Step three: and (3) cooking: the slurry A1 enters a high-concentration hydraulic pulper, a high-concentration solution c1 is added, and the reaction is carried out at the temperature of 90-100 ℃ for 60-90 minutes; under the condition of a certain pH value, adding highly concentrated solution c2, keeping the temperature at 90-100 ℃, continuing to react for 30-60 minutes, and extruding and separating pulp A2 and black liquor B2 by a pulp extruder B.

Step four: inclined tube precipitation: and (3) allowing the black liquor B1 to enter an inclined tube for precipitation to complete solid-liquid separation, allowing the lower-layer solid C to pass through a filter cake of a plate-and-frame filter press and then be sent to a boiler for combustion treatment, and returning the liquid D to the inclined tube for precipitation again to obtain the supernatant E.

Step five: two-stage DTUF (disc tube ultrafiltration): the supernatant E is firstly subjected to primary DTUF (disc tube ultrafiltration) to obtain ultrafiltration concentrated solution F1 and permeate G, wherein the ultrafiltration concentrated solution F1 enters a plate-and-frame filter press, the permeate G is subjected to DTUF (disc tube ultrafiltration) again to obtain ultrafiltration concentrated solution F2 and permeate G, the ultrafiltration concentrated solution F2 is subjected to a spray dryer to obtain a lignin product H with the molecular weight of 5000Da to 20000Da, the twice permeate G enters DTNF (disc tube nanofiltration) for desalination, and the concentrated solution F enters primary DTUF (disc tube ultrafiltration) for re-filtration.

Step six: and (3) high-concentration pulping, namely feeding the straw fiber semi-finished pulp with the concentration of 30% into a high-concentration pulping machine, and devillicating and brooming the surface of the straw fiber semi-finished pulp on the basis of keeping the fiber length as much as possible so as to improve the papermaking performance of the straw fiber semi-finished pulp.

Step seven: pulping: and the pulp A enters a high-concentration pulping machine for fibrillation to reach high-quality pulp, and the high-quality pulp is finally formed through dispatching, deslagging and a pressure screen.

Preferably, the pretreatment solution in the second step comprises the following raw materials in parts by weight: 5-10 parts of NaOH and 2-5 parts of urea.

Preferably, the weight ratio of the total amount of the black liquor B1 and the clear water to the straw fiber raw material liquor in the second step is 1: 6-10.

Preferably, the temperature of the mixing hot pre-dipping in the second step is 80-90 ℃.

Preferably, the pretreatment in the second step is carried out for 30-60 minutes.

Preferably, the highly concentrated solution c1 in the third step comprises the following raw materials in parts by weight: 5-20 parts of NaOH solution and 8-15 parts of sodium sulfite, wherein the high-concentration solution c2 comprises the following raw materials in parts by weight: 10-20 parts of hydrogen peroxide, 2-5 parts of sodium silicate, 0.2-0.5 part of magnesium sulfate and 0.1-2 parts of metal ion chelating agent (all the chemical raw materials are added in terms of calculation of absolute dry raw material quantity).

Preferably, the pH value in the step three is 10, and when the pH value is lower than 10, a small amount of NaOH can be added for regulation.

Preferably, the permeate G in the fifth step can be recycled.

Preferably, the retention molecular weight of the primary DTUF (disc tube ultrafiltration) is 20000Da, the retention molecular weight of the secondary DTUF (disc tube ultrafiltration) is 5000Da, and one or more DTUFs (disc tube ultrafiltration) with target molecular weights can be inserted between the primary DTUF (disc tube ultrafiltration) and the secondary DTUF (disc tube ultrafiltration) according to the needs.

Preferably, the black liquor B is available for the next pretreatment operation.

Compared with the prior art, the invention provides a new process for straw zero-emission pulping and lignin production, which has the following beneficial effects:

1. the novel process for straw zero-discharge pulping and lignin production integrates pulping, lignin recovery and waste water recycling, and omits the process of extraction by a high-concentration incineration method with huge investment in the traditional technology but cannot thoroughly treat pollution.

2. The novel process for pulping and producing lignin with zero discharge of straws adopts a technology of extracting and concentrating lignin in black liquor by adopting multistage DTUF (disc tube ultrafiltration) at normal pressure and within a certain temperature range, so that the lignin in the black liquor is separated from impurities and decolorized, and the permeation solution after DTNF (disc tube nanofiltration) is completely recycled, the discharge of the black liquor is zero, the pollution to the environment is greatly reduced, and social resources are saved.

3. The new process for straw zero-discharge pulping and lignin production is suitable for various straw pulping raw materials and the pulping requirements of corresponding paper varieties, and has zero discharge of papermaking wastewater.

The invention provides a zero-emission pulping process which has the advantages that under the conditions of low temperature and normal pressure, zero emission of pulping water is realized, the uniformity degree of the molecular weight distribution of extracted lignin is high, and straw pulp with stable quality is prepared.

Detailed Description

The technical solutions in the embodiments of the present invention will be clearly and completely described below, and it is obvious that the described embodiments are only a part of the embodiments of the present invention, and not all embodiments.

A new process for pulping and producing lignin with zero discharge of straws comprises the following steps:

the method comprises the following steps: preparing materials and collecting the needed agricultural straws.

Step two: pre-treating, namely, after grass crushing and dust removal are carried out on agricultural straws, fine materials are sent into pre-soaking equipment, the waste water obtained by the last cooking pulping is added into the pre-treating equipment for reuse at normal pressure and within a certain temperature range, the black liquor obtained by the last pulping at normal temperature is completely put into a pre-treating tank, meanwhile, partial clear water is supplemented, the mixture is heated for pre-soaking, and after a period of time, the pulp A1 and the black liquor B1 are separated by extrusion of a pulp extruder a.

Step three: and (3) cooking: the slurry A1 enters a high-concentration hydraulic pulper, a high-concentration solution c1 is added, and the reaction is carried out at the temperature of 90-100 ℃ for 60-90 minutes; under the condition of a certain pH value, adding highly concentrated solution c2, keeping the temperature at 90-100 ℃, continuing to react for 30-60 minutes, and extruding and separating pulp A2 and black liquor B2 by a pulp extruder B.

Step four: inclined tube precipitation: and (3) allowing the black liquor B1 to enter an inclined tube for precipitation to complete solid-liquid separation, allowing the lower-layer solid C to pass through a filter cake of a plate-and-frame filter press and then be sent to a boiler for combustion treatment, and returning the liquid D to the inclined tube for precipitation again to obtain the supernatant E.

Step five: two-stage DTUF (disc tube ultrafiltration): the supernatant E is firstly subjected to primary DTUF (disc tube ultrafiltration) to obtain ultrafiltration concentrated solution F1 and permeate G, wherein the ultrafiltration concentrated solution F1 enters a plate-and-frame filter press, the permeate G is subjected to DTUF (disc tube ultrafiltration) again to obtain ultrafiltration concentrated solution F2 and permeate G, the ultrafiltration concentrated solution F2 is subjected to a spray dryer to obtain a lignin product H with the molecular weight of 5000Da to 20000Da, the twice permeate G enters DTNF (disc tube nanofiltration) for desalination, and the concentrated solution F enters primary DTUF (disc tube ultrafiltration) for re-filtration.

Step six: and (3) high-concentration pulping, namely feeding the straw fiber semi-finished pulp with the concentration of 30% into a high-concentration pulping machine, and devillicating and brooming the surface of the straw fiber semi-finished pulp on the basis of keeping the fiber length as much as possible so as to improve the papermaking performance of the straw fiber semi-finished pulp.

Step seven: pulping: and the pulp A enters a high-concentration pulping machine for fibrillation to reach high-quality pulp, and the high-quality pulp is finally formed through dispatching, deslagging and a pressure screen.

Further, the pretreatment solution in the second step comprises the following raw materials in parts by weight: 5-10 parts of NaOH and 2-5 parts of urea, and the addition amount of the NaOH and the urea is different according to the types of oven-dried raw materials.

Further, the weight ratio of the total amount of the black liquor B1 and the clear water to the straw fiber raw material liquor in the second step is 1: 6-10.

Further, the temperature of the mixed hot pre-dipping in the second step is 80-90 ℃.

Further, the pretreatment in the second step is carried out for 30-60 minutes.

Further, the highly concentrated solution c1 obtained in the third step comprises the following raw materials in parts by weight: 5-20 parts of NaOH solution and 8-15 parts of sodium sulfite, wherein the high-concentration solution c2 comprises the following raw materials in parts by weight: 10-20 parts of hydrogen peroxide, 2-5 parts of sodium silicate, 0.2-0.5 part of magnesium sulfate and 0.1-2 parts of metal ion chelating agent. (all chemical feedstocks added above were added calculated for the amount of oven dried feedstock).

Further, the pH value in the third step is 10, and when the pH value is lower than 10, a small amount of NaOH can be added for regulation.

Furthermore, the permeate G in the fifth step can be recycled.

Further, the retention molecular weight of the primary DTUF (disc tube ultrafiltration) is 20000Da, the retention molecular weight of the secondary DTUF (disc tube ultrafiltration) is 5000Da, and one or more DTUFs (disc tube ultrafiltration) with target molecular weights can be inserted between the primary DTUF (disc tube ultrafiltration) and the secondary DTUF (disc tube ultrafiltration) according to the needs.

Further, the black liquor B may be used for the next pretreatment operation.

In the invention, the process integrates pulping, lignin recovery and waste water recycling into a whole, and saves the process of extracting by a high-concentration incineration method with huge investment in the traditional technology but not thoroughly treating pollution; by adopting the technology of extracting and concentrating the lignin in the black liquor by adopting multistage DTUF (disc tube ultrafiltration) at normal pressure and within a certain temperature range, the lignin in the black liquor is separated from impurities and decolorized, the permeation solution after DTNF (disc tube nanofiltration) is completely recycled, the black liquor discharge is zero, the pollution to the environment is greatly reduced, and social resources are saved; the method is suitable for various straw pulping raw materials and the pulping requirements of corresponding paper varieties, and zero discharge of papermaking wastewater is realized; the zero-emission pulping process for preparing the straw pulp has the advantages that under the conditions of low temperature and normal pressure, zero emission of pulping water is realized, the uniformity degree of the molecular weight distribution of the extracted lignin is high, the straw pulp with stable quality is prepared, the waste straws and other renewable resources can be utilized for papermaking in a large scale, the energy is saved, the environment is protected, the waste is changed into the valuable, and the social benefit and the economic benefit are good.

The above description is only for the preferred embodiment of the present invention, but the scope of the present invention is not limited thereto, and any person skilled in the art should be considered to be within the technical scope of the present invention, and the technical solutions and the inventive concepts thereof according to the present invention should be equivalent or changed within the scope of the present invention.