• 专利附录
  • 专利说明
  • 权利要求
  • 类似技术
  • 同族专利
  • 引用文献
  • 法律状态
  • 优先权
    • 专利摘要:
    The present invention relates to a method for optimizing chemical balance at a sulphate pulp mill producing at least chlorine dioxide bleached pulp and having a chlorine dioxide plant using at least chlorate, methanol and sulfuric acid to produce chlorine dioxide. The method comprises at least the following steps: a). gases from the system of concentrated non-condensable gases of the plant are incinerated to form a sulfur dioxide gas treated to produce concentrated sulfuric acid; and b). crude methanol from plant processes is purified to produce methanol; and c). Sodium and / or sulfur compound effluents from plant processes are used as make-up chemicals, whereby the sulfuric acid produced in step a) and methanol purified in step b) are used in the preparation of chlorine dioxide in a concentration of 94-99%, preferably 95-98%, and that in step c t ) using sesquisulphate or sodium sulfate produced by the preparation of chlorine dioxide.
    公开号:FI20175852A1
    申请号:FI20175852
    申请日:2017-09-25
    公开日:2019-03-26
    发明作者:Lauri Pehu-Lehtonen
    申请人:Andritz Oy；
    IPC主号:
    专利说明:

    METHOD FOR OPTIMIZING THE CHEMICAL BALANCE AT THE PULP MILL
    The present invention relates to a process for optimizing chemical balance at a sulphate pulp mill which produces at least a chlorine dioxide (CIO 2 ) bleached pulp and has a chlorine dioxide plant.
    The current chemical recovery scheme at the pulp mill covers the recovery and regeneration of cooking chemicals, mainly sodium hydroxide (NaOH) and sodium sulfide (Na 2 S). Nonetheless, pulp mills produce significant quantities of waste streams, 10 which are harmful to the environment but which, on the other hand, contain significant amounts of valuable sodium and sulfur, which are lost with these streams.
    These waste streams typically arise when the introduction of sulfur-containing chemicals from outside the process exceeds the amount of sulfur needed for pulping. This leads to a situation where the pulp mill has excess sulfur, which has to be eliminated from 15 processes. Typically, excess sulfur is removed as sodium sulfate (Na 2 SO 4 ) to nearby water bodies, which has been the most acceptable way to return the sulfur stream to nature. For example, the majority (80-90%) of fly ash from a recovery boiler is sodium sulphate. Traditionally, fly ash removed from the chemical cycle has been dissolved in water or condensate and led to a waste water treatment plant. Due to stricter environmental regulations, emissions of sodium sulphate have to be reduced to a large extent as they cause harm to inland waterways.
    Pulp mills use chlorine dioxide to bleach the chemical pulp. There are several commercial processes for the production of chlorine dioxide which are known per se. All processes contain sodium chlorate (NaClO 3 ) as the raw material.
    In addition, the process requires acid and a reducing agent. Typical current processes include, for example, The R8 process and the R10 process. The reducing agent is methanol (CH 3 OH) and the acid as sulfuric acid (H 2 SO 4 ). Thus, the chlorine dioxide plant is one of the major consumers of sulfuric acid and methanol at pulp mills. In addition, these chemicals are imported outside the factory because of their very high quality standards.
    The chlorine dioxide plant generates by-products containing sulfur and sodium. R8prosessissa generated acid salt sodium sesquisulfate (Na 3 H (SO 4) 2) and R10prosessissa sodium sulphate, which often can be introduced into the chemical recovery cycle, or which
    20175852 prh 25 -09- 2017 dissolved in waste water. In the latter case, the sulphate does not burden the mill's S / Nate but on the other hand increases the mill's effluent emissions. However, complete recycling of these chemicals has not been achieved, and thus the excess chemicals, mainly sulfur, that come from their introduction into the process must be removed in order to maintain the chemical balance in the process.
    It is an object of the present invention to provide a process in which the introduction of chemicals into pulp mill processes can be substantially reduced or completely stopped and thus also the need to eliminate chemicals from the process can be minimized.
    In the new process, additional chemical cycles of chemicals are formed for sulfur and / or methanol. These additional chemical cycles internally regenerate and produce refined chemicals of commercial quality, thus meeting the high quality requirements of raw materials, methanol and sulfuric acid, for example in the chlorine dioxide plant. Imports of chemicals from outside the process can be reduced, thus reducing the amount of surplus at the pulp mill, the cost of purchasing chemicals and the use of fossil chemicals.
    In the new process, the chemical balance is optimized at a sulphate pulp mill which produces at least chlorine dioxide bleached pulp and has a chlorine dioxide plant using at least chlorate, methanol and sulfuric acid to produce chlorine dioxide. The method comprises at least the following steps:
    a). the gases from the plant's concentrated non-condensable gas (CNCG) system are burned to form a gas containing sulfur dioxide (SO 2 ) which is processed to produce concentrated sulfuric acid;
    b). (a) refining methanol from crude plant processes to produce methanol; and
    c). the sodium and / or sulfur compound effluent streams from the mill processes are used as make-up chemicals wherein the sulfuric acid produced in step a) and the purified methanol in step b) are used in the production of chlorine dioxide at a concentration of 94-99%, preferably 95-98%, and in step c), sesame sulphate or sodium sulphate produced in the manufacture of chlorine dioxide is used.
    20175852 prh 25 -09- 2017
    Chlorine dioxide is prepared from sodium chlorate, sulfuric acid and methanol according to processes known per se, such as those known as R8 or R10. Such processes are described, for example, in U.S. Patents 4081520 and 5066477. According to a new process, methanol and sulfuric acid needed to produce chlorine dioxide are produced internally at the pulp mill by producing commercial grade methanol and sulfuric acid in new chemical cycles.
    According to one embodiment of the novel process, the sulfuric acid prepared in step a) is further used in at least one of the following processes: tall oil production, lignin recovery from black liquor, pulping, pH adjustment in the factory chemical recovery process, microcrystalline cellulose (MCC). Sulfuric acid is also needed in some methanol purification processes, for which internally produced acid is available. According to a preferred embodiment, the sulfuric acid produced in step a) is used in step b) if the crude methanol is acidified in the methanol purification process.
    The use of internally produced sulfuric acid reduces the amount of external sulfur feed into the chemical cycle. This also reduces the need to remove the ash from the chemical cycle of the recovery boiler.
    According to one embodiment of the process, in step c) at least one of the following effluent streams is used: soda ash, sesquisulphate or sodium sulphate for the production of chlorine dioxide, waste acid from the chlorine dioxide plant, . When internal substance streams are used as make-up chemicals, the amount of waste streams from the factory is reduced.
    On the other hand, valuable chemicals that previously had to be removed as waste to maintain chemical balance are not lost.
    As the ash removal from the recovery boiler decreases or even stops, the chlorine and potassium contained in the ash tends to be enriched in the chemical cycle, which can cause e.g. corrosion, fouling and clogging of the boiler's heating surfaces when the chlorine and potassium levels in the black liquor reach a certain level. Thus, it is advantageous to reduce the chlorine and potassium levels of the ash by appropriate treatment before recycling the ash to the process. Such treatments include, for example, ash extraction and crystallization. Sulfuric acid is also used in the ash extraction.
    20175852 prh 25 -09- 2017
    According to one embodiment of the process, the sulfuric acid produced in step a) and the methanol purified in step b) constitute at least 70%, preferably at least 80%, of the demand for these chemicals in the production of chlorine dioxide.
    According to one embodiment of the process, the purified methanol produced in step b) is further used as a nitrogen-free fuel to reduce nitrogen oxide (NO X ) emissions. Thus, the use of fossil fuels and fossil chemicals at the pulp mill can be reduced. Internally produced methanol can be used as fuel, for example, in a recovery boiler, in a lime kiln, and as a back-up fuel in a sulfuric acid plant.
    For in-house production of process chemicals, it is essential that they are of commercial quality and can therefore replace purchased chemicals. Chlorine dioxide production is a process with high purity requirements for raw material chemicals. However, purchases of sulfuric acid and fossil-based methanol can be replaced by products produced at the pulp mill when sulfuric acid is produced from the mill's non-condensable gases and methanol is produced from the crude methanol produced in the mill's pulp production process. In this case, the only purchasing chemical in the production of chlorine dioxide is sodium chlorate.
    Sulfuric acid is preferably produced by the following process. The concentrated non-condensable gases at the pulp mill are oxidized to sulfur dioxide in the incinerator.
    The gas is further treated in the presence of oxygen and a catalyst (for example, V2O5) for the oxidation of sulfur dioxide to sulfur trioxide (SO 3). The sulfur trioxide gas is condensed into the water vapor contained in the gas to form sulfuric acid. The sulfuric acid is cooled to storage temperature and excess water vapor is led to the flue gas treatment. An example of such a sulfuric acid manufacturing process is Haldor Topsoen's Wet gas Sulfuric Acid (WSA) process. The end product of the process is concentrated commercial grade sulfuric acid, since the liquefaction of the acid is 100% condensed. Concentrated commercial grade sulfuric acid can thus be produced internally at the pulp mill and significantly reduce the cost of purchasing chemicals. The concentration of sulfuric acid is 94-99%, preferably 95-98%.
    Because the sulfuric acid manufacturing process operates above the dew point of sulfuric acid, from incineration to the condenser, the metal hardware can be made from standard materials such as carbon steel without corrosion problems in the system.
    20175852 prh 25 -09- 2017
    Sulfuric acid production at the plant reduces fly ash to be removed, which is equivalent to a decrease in excess sulfur. In most cases, even the removal of surplus from the process can be completely eliminated, thus also avoiding large losses of sodium. This in turn reduces the cost of making the necessary make-up sodium hydroxide.
    Methanol is obtained as a by-product from pulp mills during the sulphate process. The resulting crude methanol contains impurities such as sulfur compounds, ethanol, ammonia and turpentine. Crude methanol is primarily obtained from the evaporation condensates of black liquor. It is also available from other pulp mill sites, such as steam and condensers from the 10 cooking stages.
    The crude methanol can be purified from sulfur compounds and other impurities to produce commercial grade methanol, for example, by the method disclosed in WO 2015/053704. The methanol content of the crude methanol is typically at least 65% by weight. The crude methanol is then washed as a nonpolar organic solvent, which treatment can be done at the pulp mill and used purified methanol in the mill processes. The solvent can be regenerated and reused. The non-polar organic solvent is typically a solvent comprising at least 50% by weight of C8-C20 alkanes and / or cycloalkanes, or comprising at least 50% by weight of triglycerides in solution at temperatures below 40 ° C.
    The solvent may be, for example, a white mineral oil, a mineral oil, a white oil, a paraffin oil or a mixture thereof. Prior to solvent treatment, the crude methanol is typically acidified with sulfuric acid and the precipitate formed, mainly ammonium sulfate ((NH) 2 SO 4 ), is removed from the methanol. Ammonium sulphate can be utilized in a biological wastewater treatment plant. In addition, turpentine may be removed and sulfur impurities removed before solvent treatment. The pretreated crude methanol is typically diluted with water prior to solvent treatment.
    Instead of the methanol purification process described above, other processes may be used to produce pure methanol.
    Commercial Methanol must meet IMPCA quality standards 30 (International Methanol Producers & Consumers Association, IMPCA Reference
    Specification) wherein the methanol is substantially sulfur and nitrogen free.
    The recycling of methanol and sulfur in the new process creates additional cycles of chemicals. The sulfuric acid plant is an additional chemical cycle in which
    20175852 prh 25 -09- 2017 Sulfur of non-condensed concentrated gases is recovered and regenerated into sulfuric acid. This creates a new kind of sulfur cycle in connection with the existing chemical cycle. Methanol, for example, is recovered, for example, from mill condensates and used purified to produce chlorine dioxide, resulting in a new methanol cycle. This sulfur cycle and the methanol cycle constitute new types of chemical cycles in the production of chlorine dioxide.
    The new method will be explained in more detail with reference to the accompanying figure, which schematically illustrates an embodiment for implementing it.
    At the sulfuric acid plant, 14 sulfuric acids are produced from the factory's concentrated non-condensable (CNCG) gases 2, which are oxidized to sulfur dioxide in the incinerator. Combustion requires support fuel 1, which may be methanol, as well as oxygen. The energy produced by the combustor is recovered as steam 7, typically intermediate pressure steam (10-45 bar). After combustion, the gas is further treated in the presence of oxygen and a catalyst (e.g., V 2 O 5 ) to oxidize sulfur dioxide to sulfur trioxide. The sulfur trioxide gas is condensed into the water vapor contained in the gas to form sulfuric acid. The sulfuric acid is cooled to storage temperature and excess water vapor is led to the flue gas treatment. The end product of the process is concentrated commercial grade sulfuric acid, since the liquefaction of the acid is 100% condensed. The concentration of sulfuric acid is 94-99%, preferably 95-98%.
    The sulfuric acid produced can be used according to a new process for the production of chlorine dioxide at the plant 15, where the sulfuric acid is fed through line 18.
    The crude methanol produced at the pulp mill is purified by a process that can produce the pure methanol needed by the chlorine dioxide plant. The process comprises the following steps at plant 16. Crude methanol 4 containing sulfur and ammonia compounds is acidified with sulfuric acid 5 to form a precipitate 13 containing ammonia sulfate. This can be utilized in a biological wastewater treatment plant as a source of microbes. Preferably, the sulfuric acid is produced at the factory as described above and is introduced from the sulfuric acid plant 14 via line 17. During acidification, crude methanol may be removed by decanting the turpentine 12. After acidification and precipitation, the methanol is distilled and the distilled methanol is diluted with water 6. The diluted methanol may be removed before the methanol is washed with a non-polar organic solvent. The washed methanol can be further removed by distillation to remove methanol, ethanol, acetone. In this way, pure methanol required for the production of chlorine dioxide can be produced from 11 in-house sources.
    The sulfur-containing gases separated during methanol purification are led through line 19 to the production of 5 sulfuric acids.
    In-house sulfuric acid and methanol are used at the chlorine dioxide plant 15 where sulfuric acid is fed through line 18 and methanol is fed through line 20. For example, chlorine dioxide 9 is produced by processes known per se, R8 or R10, sodium chlorate 3 produces sulfur10 and sodium-containing by-products 10. The R8 process also produces acidic salt,
    In addition, sulfuric acid 8 can also be used, for example, at a possible tall oil plant, for lignin recovery from black liquor, for pulp bleaching.
    In addition, purified methanol 11 can also be used as a back-up fuel 1 for a sulfuric acid plant, as a fuel in a recovery boiler and / or in a lime kiln.
    权利要求:
    Claims (6)
    [1]
    CLAIMS:
    A method for optimizing the chemical balance of a sulfate pulp mill producing at least a chlorine dioxide bleached pulp and having a chlorine dioxide plant using at least chlorate, methanol and
    5 sulfuric acids for the preparation of chlorine dioxide, the process comprising at least the following steps:
    a). the gases from the plant's system of concentrated non-condensable gases are burned to form a sulfur dioxide-containing gas which is treated to produce concentrated sulfuric acid;
    10 b). (a) refining methanol from crude plant processes to produce methanol; and
    c). the sodium and / or sulfur compounds effluent streams from the mill processes are used as make-up chemicals using sulfuric acid produced in step a) and
    The methanol purified in step b) has a sulfuric acid concentration of 94-99%, preferably 95-98%, and the sesquis sulfate or sodium sulfate produced in the step c) is used.
    [2]
    Process according to claim 1, characterized in that the sulfuric acid prepared in step a) is additionally used in at least one
    20 of the following processes: tall oil production, lignin recovery from black liquor, pulp bleaching, pH adjustment in the factory chemical recovery process, microcrystalline cellulose production.
    [3]
    Method according to claim 1 or 2, characterized in that in step c) at least one of the following discharge streams is used:
    25 ash from boiler soda ash, sesame sulphate or sodium sulphate from the manufacture of chlorine dioxide, waste acid from the chlorine dioxide plant, alkaline filtrates from the pulp bleaching plant.
    [4]
    Process according to Claim 1,2 or 3, characterized in that sulfuric acid and methanol constitute at least 70% of these chemicals.
    30 needs in the production of chlorine dioxide.
    [5]
    A process according to any one of the preceding claims, characterized in that the purified methanol produced in step b) is further used as a nitrogen-free fuel to reduce nitrogen oxide emissions.
    [6]
    A process according to any one of the preceding claims, characterized in that in step a) the sulfur dioxide-containing gas is treated in the presence of oxygen and a catalyst to oxidize the sulfur dioxide to sulfur trioxide, which is condensed into water vapor to produce concentrated sulfuric acid.
    类似技术:
    公开号 | 公开日 | 专利标题
    FI105215B|2000-06-30|A method for treating odor gases in a pulp mill
    FI111168B|2003-06-13|Process for pulp leaching without using chlorine-containing chemicals
    EP2203589B1|2017-01-18|Method in the treatment of odorous gases of a chemical pulp mill
    EP1524241B1|2009-08-26|A method for producing sodium dithionite to be used in the bleaching of mechanical pulp
    US8440159B2|2013-05-14|Method for extracting ammonium salt and methanol from a liquid obtained from foul condensates in a cellulose pulp mill
    RU2067637C1|1996-10-10|Method for preparation of cooking liquor for cellulose sulfate digestion
    FI64408C|1983-11-10|SAETT VIDEO UPPSLUTNING AV CELLULOSAHALTIGT MATERIAL
    US3755068A|1973-08-28|Regeneration of chlorine dioxide for pulp treatment
    FI20175852A1|2019-03-26|Method of controlling the chemical balance of a pulp mill
    FI119915B|2009-05-15|Removal of sulfur from the smell gases of a cellulose factory
    RU2675454C2|2018-12-19|Method for handling spent wash solution of lignin-recovery process
    US8152956B2|2012-04-10|Use of chemical pulp mill steam stripper off gases condensate as reducing agent in chlorine dioxide production
    US4508593A|1985-04-02|Process for recovery of sulfur dioxide liberated in the chemical pulping of lignocellulosic material
    EP2920359B1|2016-09-14|Method for leaching recovery-boiler ash
    FI116074B|2005-09-15|Sulfur recovery in a sulfate cellulose process
    EP1424435B1|2007-07-04|Method of reducing nitrogen oxide emissions in a chemical pulp mill
    Kilpi2019|Reduction of sulfate emissions in bleached softwood kraft pulp mill
    US20200291574A1|2020-09-17|A method and a system for adjusting s/na -balance of a pulp mill
    SE510171C2|1999-04-26|Process for the collection and reuse of sulfur in a cellulose plant
    FI115229B|2005-03-31|A method for reducing the corrosion of a pulp mill power boiler
    FI115471B|2005-05-13|Procedures for the treatment of liquids
    CN113474510A|2021-10-01|Method for compensating for sodium loss in a pulp mill, method and system for producing bleached cellulose pulp
    FI20176188A1|2019-06-30|A method and a system for adjusting S/Na -balance of a pulp mill
    同族专利:
    公开号 | 公开日
    BR112020005280A2|2020-09-24|
    US20200283954A1|2020-09-10|
    FI129150B|2021-08-13|
    EP3688219A1|2020-08-05|
    RU2020111790A3|2021-12-17|
    JP2020535329A|2020-12-03|
    RU2020111790A|2021-10-27|
    CN111212945A|2020-05-29|
    CA3075496A1|2019-03-28|
    WO2019058032A1|2019-03-28|
    CL2020000704A1|2020-07-31|
    引用文献:
    公开号 | 申请日 | 公开日 | 申请人 | 专利标题
    US2881052A|1953-06-08|1959-04-07|Allied Chem|Production of chlorine dioxide|
    CA1080434A|1976-03-19|1980-07-01|Richard Swindells|High efficiency chlorine dioxide production using hc1 as acid|
    SE442523B|1981-06-22|1986-01-13|Mo Och Domsjoe Ab|PROCEDURE FOR PREVENTING EMISSIONS OF SULFUR INHALING GASES IN THE PREPARATION OF CHEMICAL CELLULOSAMASSA|
    SE463669B|1988-06-17|1991-01-07|Eka Nobel Ab|PROCEDURE FOR PREPARATION OF CHLORIDE Dioxide|
    SE463670B|1988-10-11|1991-01-07|Eka Nobel Ab|PROCEDURE FOR PREPARATION OF CHLORIDE Dioxide|
    US5116595A|1991-04-22|1992-05-26|Tenneco Canada Inc.|Metathesis of acidic by-product of chlorine dioxide generating process|
    US5300191A|1992-07-30|1994-04-05|Kamyr, Inc.|Chlorine dioxide generation for a zero discharge pulp mill|
    CA2219550C|1996-11-01|2008-05-06|Sterling Canada, Inc.|A method of recovery of chemical compounds from a pulp mill|
    CA2707024C|2007-12-26|2013-04-09|Fpinnovations|Use of chemical pulp mill steam stripper off gases condensate as reducing agent in chlorine dioxide production|
    FI20135105A|2013-02-04|2014-08-05|Andritz Oy|METHOD FOR RECOVERY OF CHEMICALS AND BY-PRODUCTS FROM HIGH SULFIDITY COOKERS|
    法律状态:
    2021-08-13| FG| Patent granted|Ref document number: 129150 Country of ref document: FI Kind code of ref document: B |
    优先权:
    申请号 | 申请日 | 专利标题
    FI20175852A|FI129150B|2017-09-25|2017-09-25|Method of controlling the chemical balance of a pulp mill|FI20175852A| FI129150B|2017-09-25|2017-09-25|Method of controlling the chemical balance of a pulp mill|
    PCT/FI2018/050691| WO2019058032A1|2017-09-25|2018-09-25|Method of controlling the chemical balance of a pulp mill|
    EP18801009.4A| EP3688219A1|2017-09-25|2018-09-25|Method of controlling the chemical balance of a pulp mill|
    RU2020111790A| RU2020111790A3|2017-09-25|2018-09-25|
    CA3075496A| CA3075496A1|2017-09-25|2018-09-25|Method of controlling the chemical balance of a pulp mill|
    US16/649,819| US20200283954A1|2017-09-25|2018-09-25|Method of controlling the chemical balance of a pulp mill|
    BR112020005280-9A| BR112020005280A2|2017-09-25|2018-09-25|chemical balance control method of a pulp mill|
    CN201880062121.5A| CN111212945A|2017-09-25|2018-09-25|Method for controlling chemical equilibrium of pulp mill|
    JP2020537877A| JP2020535329A|2017-09-25|2018-09-25|How to control the chemical balance of a pulp mill|
    CL2020000704A| CL2020000704A1|2017-09-25|2020-03-18|Method to control the chemical balance of a pulp mill.|
    [返回顶部]