• 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 invention relates to a method for heating a moving biomass in an industrial treatment path comprising an inlet (1) for the incoming biomass, a heating means (4) and a treatment station (5), a fraction of the biomass heated by the heating means (4) being returned by a return branch (R) to a mixing station (2) upstream of the heating means (4) to form therewith the incoming biomass a mixture having a temperature above the temperature of the incoming biomass, the heated biomass fraction being taken at an outlet (51) of the treatment station (5).
    公开号:FR3027914A1
    申请号:FR1460617
    申请日:2014-11-04
    公开日:2016-05-06
    发明作者:Pierre Emmanuel Pardo；Jean-Louis Bourdais
    申请人:Degremont SA；
    IPC主号:
    专利说明:

    [0001] The present invention relates to the field of the thermal and chemical treatment of a biomass such as sludge from a treatment sector. used waters.
    [0002] The present invention more particularly relates to a method of hydrothermal carbonization of a biomass and a device for implementing such a method. STATE OF THE PRIOR ART In the prior art, a hydrothermal carbonization process is known, typically consisting in subjecting a biomass to a temperature close to 200 ° C. and at a pressure close to 20 bars. EP 2 388 305 A2 describes an installation comprising a treatment path in which a biomass is circulated, this path comprising in particular a heat exchanger and a reactor. The heat exchanger is arranged to heat the biomass circulating in the path through a transfer circuit in which circulates a transfer fluid. After having been preheated in this heat exchanger, the biomass is then carbonized in the reactor in which it performs an average residence time of about 4 hours. Patent EP 2,388,305 A2 furthermore reports test results according to which the injection of an additive such as glycerine into the biomass makes it possible to significantly reduce the viscosity of this biomass and to significantly promote the rise in temperature of the mixture comprising the biomass and the additive within the reactor. Such an installation or such a hydrothermal carbonization process has several drawbacks: the reactor must supply energy to increase the temperature of the biomass; the residence time of the biomass within the reactor involves stirring the reactor; biomass within the reactor to ensure heat exchange and homogenize the heating, - the temperature gradient between the heating surface of the reactor and the biomass promotes the sedimentation of the biomass, leading to implement a mixer-wiper in order to eliminate the deposition of the biomass on the internal walls of the reactor, the mixer-wiper also involving maintenance costs and further constituting a room at risk for the personnel and a room decreasing the reliability of the installation, - the inherent residence time heating the biomass in the reactor limits the volume of biomass that the facility can process and imposes to increase the volume the reactor to process more biomass, - the rise in temperature of the biomass within the heat exchanger is limited by the relatively high viscosity of the biomass entering the installation; as an indication, a dewatered sludge is at least ten times more viscous than water, - the thermal characteristics of a sewage sludge biomass imply significant injection pump powers and therefore an important cost of electrical energy. The present invention is intended in particular to overcome all or part of these disadvantages by proposing a method for heating a biomass, as well as a device for implementing such a method, optimizing the heat exchange and exploiting the thermal energy produced by the implementation of such a method or the operation of such a device.
    [0003] SUMMARY OF THE INVENTION To this end, the present invention proposes a method for heating a biomass moving in an industrial treatment path comprising an inlet for the incoming biomass, a heating means and a treatment station, a fraction of the biomass. heated by the heating means being returned by a return branch to a mixing station upstream of the heating means to form therewith the incoming biomass a mixture having a temperature above the temperature of the incoming biomass, the heated biomass fraction being taken at an outlet of the treatment station.
    [0004] Such a method makes it possible to reduce the viscosity of the biomass upstream of the heating means compared with a method that does not carry out such a return. This results in a reduction in the pressure drop in the path and an improvement in the heat exchange gain at the heating means. This results in a greater increase in temperature of the biomass. Advantageously, the biomass is a sewage sludge, preferably dehydrated, and the treatment is a hydrothermal carbonization.
    [0005] Indeed, sewage sludge, especially dehydrated, has relatively poor heat exchange coefficients, that is to say, disadvantaging its rise in temperature and involving very large equipment sizes. The method according to the invention makes it possible to improve the exchange coefficients of such a sludge.
    [0006] According to a particularly advantageous characteristic, the heating means is controlled by means of a control means so that the temperature of the biomass reaches a parameterized temperature before it arrives in the treatment station, the parameterized temperature being between 165.degree. C and 205 ° C, preferably 185 ° C. In this way, the temperature of the biomass upon arrival at the treatment station is sufficiently high, particularly when the treatment is a hydrothermal carbonization, to avoid having to further increase the temperature of the biomass within the treatment station . This eliminates the heating function of the treatment station, and thus eliminate the temperature gradient in the treatment station resulting from such a function. Consequently, a process provided with such a characteristic makes it possible to limit the bonding by baking (or depositing) of the biomass on the walls of the treatment station, such a bonding or deposit which can lead to an interruption of the heat exchange in - 4 - the treatment station. It also makes it possible to dispense with any means or operation intended to limit such gluing or deposition (for example, a scraping and / or mixing operation). Another advantage of the elimination of the heating function of the treatment station is that, for a given quantity of biomass to be treated, the volume of the treatment station can be reduced, because the residence time of the biomass, in the station of treatment, associated with the heating function is no longer necessary.
    [0007] According to a first variant of the invention, the biomass is put under pressure between the mixing station and the heating means, and the pressure of the biomass fraction is lowered in the return branch. The relaxation of the biomass fraction circulating in the return branch generates vapor that propagates in the incoming biomass in the mixing station and condenses as it migrates by heating the incoming biomass. The condensation of the vapor of this fraction of biomass circulating in the return branch is made possible by the fact that the biomass in the mixing station is under the influence of atmospheric pressure, the mixture being pressurized in the flow path. downstream of the mixing station. In addition, the vibration generated by the trigger prevents the biomass located in the mixing station from bowing, promoting mixing. According to one particularity of the invention, the fraction of expanded biomass and the incoming biomass undergo a mechanical mixing operation (for example using a mixer). Such an operation further promotes mixing. Advantageously, the flow rate of the biomass fraction returned to the mixing station is adjusted according to the amount of incoming biomass contained in the mixing station. According to a particular feature, the return of biomass fraction is piloted so that this fraction is effectively returned to the mixing station only when incoming biomass is present in the mixing station. According to a second variant of the invention, the biomass is pressurized upstream of the mixing station, and the pressure of the fraction is raised in the return branch. This second variant has the advantage of returning the fraction 5 of biomass in the path by mixing it with the incoming biomass already pressurized, avoiding the use of an energy sink to lower the pressure of the fraction in the branch. back. According to an advantageous characteristic, the pressure of the biomass upstream of the heating means is raised to a value making it possible to heat the mixture to a temperature above 100 ° C. without boiling. According to another advantageous characteristic, the pressure at the output of the pressurizing pump is greater than 3 MPa. These characteristics make possible a controlled rise in the temperature of the biomass. Advantageously, according to a first variant of the invention, the path also comprises a cooling station downstream of the treatment station, and a transfer fluid is heated in its path between the cooling station and the heating means. Very advantageously, the transfer fluid is heated to a temperature higher than that of the biomass at the treatment station. The heat transferred to the heating means can thus heat the biomass to said parameterized temperature prior to arrival at the treatment station. According to a very advantageous characteristic, the same external heat source is used to heat the transfer fluid and a heat transfer fluid ensuring a temperature maintenance of the biomass at the treatment station. Advantageously, the external heat source may consist of a boiler burner. According to a second advantageous variant of the invention, heat is recovered from the biomass downstream of the treatment station and this recovered heat is transferred to the biomass upstream of the treatment station.
    [0008] According to an advantageous characteristic of the invention, the method comprises a step of injecting an additive into the biomass upstream of the heating means. The injected additive may consist of any catalyst capable of decomposing the organic material, for example an acid such as sulfuric acid or a catalyst as described in patent EP 2 388 305 A2. Such an injection step also contributes to lowering the viscosity of the biomass and thus promoting its rise in temperature, and also reduces the fouling phenomena in the path. Alternatively, the injection step may be carried out downstream or within the heating means. According to another advantageous characteristic of the invention, a part of the biomass is taken from the treatment station by means of a recirculation branch and this part is returned to the treatment station so as to generate a movement of the biomass. in the treatment station. Such removal and return of biomass part in the treatment station limits the sticking or deposition of biomass in the treatment station, and to overcome any means or operation to limit such bonding or deposit. Advantageously, the portion of biomass is sampled at a flow rate of between 5 and 15 times the flow of biomass entering the treatment station. The invention also relates to a device for implementing a method according to various combinations of the characteristics which have just been described, this device comprising an industrial processing path comprising: an input arranged to bring in the biomass entering the path, a pressurizing pump arranged to move the biomass in the path, a heating means capable of heating the biomass, a treatment station capable of maintaining the biomass substantially at a temperature of entry into the station of treatment, the treatment station being installed downstream of the heating means, an at least indirect heat exchange means between the biomass leaving the treatment station and the biomass flowing in the path upstream of the treatment station, a branch return device capable of transferring a fraction of biomass from an outlet of the treatment station to a mixing station. Preferably, the device further comprises injection means capable of injecting an additive into the path.
    [0009] According to an advantageous characteristic, the heat exchange means comprises: a transfer circuit in which circulates a transfer fluid so as to heat the biomass in the heating means by heat exchange between the transfer fluid and the biomass, and means for circulating the transfer fluid, preferably a pump, able to circulate the transfer fluid in the transfer circuit.
    [0010] According to another advantageous characteristic, the device further comprises an external heat source arranged to heat the transfer fluid and a coolant flowing in an envelope of the treatment station. According to yet another advantageous characteristic, the return branch comprises a pressure lowering device, preferably an expander, for example of the diaphragm or pump or valve type, of the biomass circulating in the return branch.
    [0011] Very advantageously, the biomass enters the treatment station by a lower part and leaves an upper part. A biomass, especially when it consists of sewage sludge, is denser than the surrounding water. The solid fraction, surrounded by undissolved organic matter, will therefore tend to have a gravitational effect at a lower altitude compared to the already solubilized fractions and therefore for which the carbonization reactions are in progress or have already taken place. The residence time of a fraction of non-carbonized biomass in the treatment station is thus increased, compared to a device that enters the biomass through an upper part and makes it exit through a lower part. The relative increase in residence time of the biomass in the treatment station increases the quality of the treatment.
    [0012] According to a very advantageous characteristic, the device according to the invention further comprises a recirculation branch arranged to withdraw a portion of biomass in the treatment station and to return this portion of biomass in the treatment station.
    [0013] Very advantageously, the treatment station comprises a partition arranged to convey to the return branch a fraction of liquid biomass. The presence of mineral materials in the biomass fraction circulating in the return branch is thus limited, which reduces the risk of damage by abrasion, in particular of the pressurizing pump and the heating means. According to an advantageous characteristic, the treatment station is mechanically passive, that is to say not having a scraper or mixer. - 9 - Such parts are risky parts for the personnel and the availability of the installation. Advantageously, the treatment station is a hydrothermal carbonization reactor for sewage sludge. DESCRIPTION OF THE FIGURES AND EMBODIMENTS Other advantages and particularities of the invention will appear on reading the detailed description of implementations and non-limiting embodiments, and the following appended drawings: FIG. 1 is a view schematic of a hydrothermal carbonization device according to the invention comprising a pressurizing pump between a mixing station and a heating means, - FIGURE 2 is a schematic view of a hydrothermal carbonization device according to the invention comprising a pressurizing pump upstream of the mixing station; FIGURES 3a, 3b and 3c are schematic views of a treatment station comprising: o a siphoid partition (FIGURE 3a), o a deflector (FIGURE 3b), o a recirculation outlet in the up position (FIGURE 3c) - FIGURE 4 is a schematic view of a hydrothermal carbonization device according to the invention comprising a heat exchange means direct. The embodiments described below being in no way limiting, it will be possible to consider variants of the invention comprising only a selection of characteristics described, isolated from the other characteristics described (even if this selection is isolated within a sentence including these other characteristics), if this selection of features is sufficient to confer a technical advantage or to differentiate the invention from the state of the prior art. This selection comprises at least one characteristic, preferably functional without structural details, or with only a portion of the structural details if this portion alone is sufficient to confer a technical advantage or to differentiate the invention from the state of the art. the prior art.
    [0014] FIGURE 1 illustrates a preferred embodiment of the invention. According to this embodiment, the device according to the invention comprises an industrial treatment path in which biomass circulates. Incoming biomass, for example dewatered sewage sludge, enters through an inlet 1 in the path where it is introduced into a mixing station 2. The mixing station 2 is preferably a closed silo capable of containing a quantity of water. of biomass of several cubic meters, under atmospheric pressure. The mixing station 2 preferably comprises a feed pump (not shown) for filling the mixing station 2 with biomass and a feed screw (not shown) arranged to introduce biomass contained in the mixing station 2 to the mixing station 2. in a pipe connecting the mixing station 2 to a heating means 4, this pipe comprising between the mixing station 2 and the heating means 4 a pressurizing pump 3. The pressurizing pump 3 allows circulate the biomass in the path. More specifically, the pressurizing pump 3 is of a type capable of raising the pressure of the biomass at the pump outlet 3 to a value greater than 3 MPa (piston pump, diaphragm pump or other). Under the effect of the pressurizing pump 3, the biomass is conveyed from the pressurizing pump 3 to the heating means 4. The heating means 4 is preferably a heat exchanger. This heating means 4 makes it possible to heat the biomass by heat exchange between a transfer fluid flowing in a transfer circuit T and the biomass passing through the heating means 4. To do this, the transfer fluid, for example from the oil, is itself heated by means of an external heat source T3, this heat source being for example a boiler burner.
    [0015] Piping also connects the heating means 4 to a treatment station 5 to which the biomass is conveyed. The treatment station 5 is preferably a reactor comprising a chamber capable of receiving biomass and maintaining this biomass at a pressure typically of between 2 and 3 MPa. In a preferred embodiment, the unique function of the treatment station 5 is to provide a residence time for subjecting the biomass to chemical reactions, typically hydrolysis. For this reason, the treatment station 5 may alternatively consist of a reactor, baffled or not, cased or not, or for example a tube of sufficient length to ensure the required residence time. According to the embodiment shown in FIGURES 1 and 2, the biomass from the heating means 4 enters the chamber of the treatment station 5 via a lower part 53, ie a part of the treatment station. 5 whose altitude is substantially the lowest relative to the implantation of the treatment station 5 in the room housing the device. According to the embodiments of FIGURES 1 and 2, a pipe 20 also connects the treatment station 5 to a cooling station 6. According to these same embodiments, after a residence time, the biomass (hydrolysed) leaves the chamber of the treatment station 5 by an upper part 54 from which it is conveyed to the cooling station 6. By the upper part 54, is meant a portion 25 of the treatment station 5 whose altitude is substantially the highest relative to the implantation of the treatment station 5 in the room housing the device, as opposed to the lower part 53. Alternatively, the biomass can also enter the treatment station 5 by an upper part and leave it by a lower part. According to yet another alternative, the biomass may also enter the treatment station 5 by a lower part and be conveyed from this lower part to an upper part of the chamber by a pipe, the biomass may leave the post chamber treatment 5 by a lower part. A fraction of biomass contained in the treatment station 5 is transferred to the mixing station 2 by a return branch R. This transferred biomass fraction is preferably taken at an outlet 51 of the treatment station 5 arranged so that the biomass fraction taken preferably contains a liquid portion rather than a solid portion. Different means are preferably used to collect such a fraction.
    [0016] In the example shown in FIGURE 3a, the chamber comprises a siphoid partition Cl requiring the biomass to change direction before reaching the exit 51 (located at low altitude). Such a partition C1 causes a decrease in the solid portion (represented by arrows in solid lines) in the recirculated fraction, the inertia of the solid portion favoring the liquid portion selection phenomenon (represented by dashed arrows) to constitute the biomass fraction arriving at the outlet 51. In another example shown in FIGURE 3b, the outlet 51 is located at an average altitude and the selection of liquid portion is carried out using a deflector type partition C2.
    [0017] In the example shown in FIG. 3c, the outlet 51 is situated at a relatively high altitude, naturally favoring the selection of a liquid portion to constitute the fraction of biomass conveyed towards this outlet 51. As represented in FIG. 1, the fraction of circulating biomass in the return branch R is subjected to the action of a pressure lowering device R1 before its arrival in the mixing station 2. This pressure lowering device R1 is for example a diaphragm-type expansion valve, pump or valve. The arrival of the expanded biomass fraction by the pressure lowering device R1 is preferably located above the feed screw. Preferably, the flow rate of the biomass fraction passing through the pressure-reducing device R1 is adjusted by any appropriate control means C so that this flow rate is non-zero only if the mixing station 2 contains a quantity sufficient incoming biomass, for example over a height of 1 to 2 meters. The pressure lowering device R1 thus relaxes the biomass fraction taken from the treatment station 5, which has the effect of creating a vapor of this biomass fraction, which is propagated in the incoming biomass contained in the mixing station. 2 by condensing and warming up this incoming biomass. If necessary, it is intended to add a mixer (not shown) in addition to the feed screw.
    [0018] The cooling station 6 is preferably a heat exchanger. The cooling station 6 makes it possible to cool the biomass leaving the treatment station 5 by heat exchange between the transfer fluid 15 flowing in the transfer circuit T and the biomass passing through this cooling station 6. Thus, the transfer circuit T connects the heating means 4 at the cooling station 6. It thus constitutes, with the heating means 4 and the cooling station 6, a heat exchange means between the biomass leaving the treatment station 5 and the biomass flowing in the path upstream of the treatment station 5. As shown in FIGURES 1 and 2, the transfer fluid is circulated in the transfer circuit T by circulation means Ti, typically a pump. An external heat source T3, for example a boiler burner, heats the transfer fluid at the heat exchanger T2. The biomass circulating in the heating means is heated by the transfer fluid and heated from which it takes part of its heat. The transfer fluid also recovers a part of the heat of the biomass circulating in the cooling station 6. Alternatively, according to an embodiment shown in FIG. 4, part of the heat of the biomass circulating in the path downstream of the Treatment station 5 is transferred to the circulating biomass in a heat recovery unit 4a installed upstream of the heating means 4b. In this case, the heat exchange means carries out a direct heat exchange between the biomass leaving the treatment station 5 and the biomass circulating in the path upstream of the treatment station 5, via the recuperator heat 4a.
    [0019] In a preferred embodiment, the chamber of the treatment station 5 is surrounded by a casing 52 in which a coolant is circulated. This coolant is heated and maintained at a temperature capable of maintaining the biomass contained in the chamber at its temperature before entering the treatment station 5, that is to say when the biomass was between the means of heating 4 and the treatment station 5, and able to compensate for thermal losses related to the structure of the treatment station 5.
    [0020] Heating of the heat transfer fluid is preferably carried out by the same external heat source T3 as that heating the transfer fluid, at the level of the heat exchanger T2. The transfer fluid and the coolant can thus be a same fluid, for example oil, circulating in a circuitry arranged to heat the transfer fluid (flowing in the circuit T) and the heat transfer fluid (flowing in the envelope 52) at the desired temperatures. The differential control of the temperature of the transfer fluid and the coolant is carried out by any appropriate means, for example valves (not shown) mounted on said circuitry and a control of the opening and closing of these valves and the heat source T3. In order to raise the temperature of the biomass in the path of the heating means 4, the device is piloted, for example by the control means C, so that the heat source T 3 raises the transfer fluid to a temperature greater than that of the biomass contained in the treatment station 5, for example at a temperature close to 210 ° C. To limit the phenomenon of biomass deposition on the walls of the chamber of the treatment station 5 while using a mechanically passive treatment station (i.e. without scraper and / or mixer), the station - 15 treatment 5 preferably comprises a recirculation branch M for circulating the biomass in the chamber. To do this, biomass is preferably aspirated in the upper part 54 (the biomass being more liquid) and this biomass is reinjected into the chamber by a lower part 53. Preferably, the flow rate of this recirculation is dimensioned so that the biomass circulating in the recirculation branch M is withdrawn at a flow rate of between 5 and 15 times the flow rate of biomass entering the treatment station 5 from the heating means 4. Such a recirculation ensures a good homogeneity of the temperature. the biomass contained in the treatment station 5. The circulation of this biomass in the recirculation branch M is preferably provided by a diaphragm pump M1, preferably sealed and offset from the treatment station 5. Such a pump M1 thus installed increases the reliability of the device, this pump M1 15 can for example be repaired or maintained without involving putting the dispositi f out of order in its entirety. Preferably, an additive is injected into the biomass in the path, preferably upstream of the heating means 4, 4b, by any suitable injection means 7, in order to further reduce the viscosity of the biomass. It can be seen that the various solutions proposed by the present invention make it possible to reduce the viscosity of the biomass and consequently to promote the increase of its temperature by reduced means. The surface of the heat exchangers (heating means 4, 4b and / or cooling station 6), the pipe diameters as well as the volume of the treatment station 5 can thus be reduced.
    [0021] In an embodiment shown in FIGURE 2, the pressurizing pump 3b is installed between the inlet 1 and the mixing station 2. In this latter configuration (FIGURE 2), the biomass circulating in the return branch R is introduced at a point in the path subjected to a pressure greater than atmospheric pressure. A lifting pump R2 is thus installed in the return branch R in order to withstand the pressure drop that is implied by the implementation of the return branch R. In an embodiment not shown, the lifting pump R2 is installed between the mixing station 2 and the heating means 4.
    [0022] Of course, the invention is not limited to the examples which have just been described and numerous adjustments can be made to these examples without departing from the scope of the invention. In addition, the various features, shapes, variants and embodiments of the invention can be associated with each other in various combinations in that they are not incompatible or exclusive of each other.
    权利要求:
    Claims (23)
    [0001]
    REVENDICATIONS1. Method for heating a moving biomass in an industrial treatment path having an inlet (1) for the incoming biomass, a heating means (4, 4b) and a treatment station (5), characterized in that a fraction of the biomass heated by the heating means (4, 4b) is returned by a return branch (R) to a mixing station (2) upstream of the heating means (4, 4b) to constitute therewith the biomass entering a mixture having a temperature above the temperature of the incoming biomass, the heated biomass fraction being taken at an outlet (51) of the treatment station (5).
    [0002]
    2. Method according to claim 1, characterized in that the biomass is a sewage sludge and the treatment is a hydrothermal carbonization.
    [0003]
    3. Method according to claim 1 or 2, characterized in that the heating means (4, 4b) is controlled by means of a control means (C) so that the temperature of the biomass reaches a parameterized temperature. before reaching the treatment station (5), the set temperature being between 165 ° C and 205 ° C, preferably 185 ° C.
    [0004]
    4. Method according to one of claims 1 to 3, characterized in that the biomass is pressurized between the mixing station (2) and the heating means (4, 4b), and in that it lowers the pressure of the biomass fraction in the return branch (R).
    [0005]
    5. Method according to claim 4, characterized in that the flow rate of the biomass fraction returned to the mixing station (2) is adjusted according to the amount of incoming biomass contained in the mixing station (2).
    [0006]
    6. Method according to one of claims 1 to 3, characterized in that the biomass is pressurized upstream of the mixing station (2), and in that the pressure of the fraction is raised in the branch. back (R) .- 18 -
    [0007]
    7. Method according to one of claims 4 to 6, characterized in that raises the pressure of the biomass upstream of the heating means (4, 4b) to a value for heating the mixture to a higher temperature at 100 ° C without boiling.
    [0008]
    8. Process according to claim 7, characterized in that the pressure at the outlet of the pressurizing pump (3, 3b) is greater than 3 MPa.
    [0009]
    9. Method according to one of claims 1 to 8, characterized in that the path further comprises a cooling station (6) downstream of the treatment station (5), and in that it heats a transfer fluid in its path between the cooling station (6) and the heating means (4).
    [0010]
    10. Process according to claim 9, characterized in that the transfer fluid is heated to a temperature higher than that of the biomass at the treatment station (5).
    [0011]
    11. A method according to claim 9 or 10, characterized in that the same external heat source (T3) is used to heat the transfer fluid and a heat transfer fluid that maintains the temperature of the biomass at the treatment station ( 5).
    [0012]
    12. Process according to one of Claims 1 to 8, characterized in that biomass heat is recovered downstream from the treatment station (5) and this recovered heat is transferred to the biomass in question. upstream of the treatment station (5).
    [0013]
    13. Method according to one of claims 1 to 12, characterized in that it comprises a step of injecting an additive into the biomass upstream of the heating means (4, 4b).
    [0014]
    14. Method according to one of claims 1 to 13, characterized in that a part of the biomass is taken from the treatment station (5) by means of a recirculation branch (M) and this part is returned. in the treatment station (5) so as to generate a movement of the biomass in the treatment station (5).
    [0015]
    15. Process according to claim 14, characterized in that the portion of biomass is sampled at a flow rate of between 5 and 15 times the flow of biomass entering the treatment station (5).
    [0016]
    16. Apparatus for carrying out a method according to one of claims 1 to 15, characterized in that it comprises an industrial treatment path comprising: an inlet (1) arranged to enter the incoming biomass in the path, a pressurizing pump (3) arranged to move the biomass in the path, a heating means (4, 4b) capable of heating the biomass, a treatment station (5) capable of maintaining the biomass substantially at an inlet temperature in the treatment station (5), the treatment station (5) being installed downstream of the heating means (4), at least one indirect means of heat exchange between the outgoing biomass of the treatment station (5) and the biomass circulating in the path upstream of the treatment station (5), a return branch (R) able to transfer a biomass fraction from an outlet (51) of the treatment station (5). ) to a mixing station (2). 25
    [0017]
    17. Device according to claim 16, characterized in that the heat exchange means comprises: a transfer circuit (T) in which a transfer fluid circulates so as to heat the biomass in the heating means (4, 4b ) By heat exchange between the transfer fluid and the biomass, and means for circulating (Ti) the transfer fluid able to circulate the transfer fluid in the transfer circuit (T).
    [0018]
    18. Apparatus according to claim 17, characterized in that it further comprises an external heat source (T3) arranged to heat the transfer fluid and a coolant circulating in an envelope (52) of the station. treatment (5).
    [0019]
    19. Device according to one of claims 16 to 18, characterized in that the return branch (R) comprises a device for lowering the pressure (R1) of the biomass circulating in the return branch (R).
    [0020]
    20. Device according to one of claims 16 to 19, characterized in that the biomass enters the treatment station (5) by a lower portion (53) and exits through an upper portion (54).
    [0021]
    21. Device according to one of claims 16 to 20, characterized in that the treatment station (5) comprises a partition (C1, C2) arranged to convey to the return branch (R) a liquid biomass fraction. 15
    [0022]
    22. Device according to one of claims 16 to 21, characterized in that the processing station (5) is mechanically passive.
    [0023]
    23. Device according to one of claims 16 to 22, characterized in that the treatment station (5) is a hydrothermal carbonization reactor for sewage sludge.
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    同族专利:
    公开号 | 公开日
    US10287505B2|2019-05-14|
    EP3287510B1|2019-08-14|
    US20170233659A1|2017-08-17|
    EP3146026A1|2017-03-29|
    EP3287510A1|2018-02-28|
    CN106536691A|2017-03-22|
    AU2015341447B2|2020-02-27|
    AU2015341447A1|2017-01-19|
    FR3027914B1|2018-05-04|
    WO2016071808A1|2016-05-12|
    CN106536691B|2020-07-14|
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    优先权:
    申请号 | 申请日 | 专利标题
    FR1460617|2014-11-04|
    FR1460617A|FR3027914B1|2014-11-04|2014-11-04|METHOD FOR HYDROTHERMAL CARBONIZATION OF BIOMASS, AND DEVICE THEREFOR|FR1460617A| FR3027914B1|2014-11-04|2014-11-04|METHOD FOR HYDROTHERMAL CARBONIZATION OF BIOMASS, AND DEVICE THEREFOR|
    CN201580039403.XA| CN106536691B|2014-11-04|2015-10-29|Method for hydrothermal carbonization of biomass and related apparatus|
    EP15798565.6A| EP3146026A1|2014-11-04|2015-10-29|Method for the hydrothermal carbonisation of a biomass and associated device|
    EP17195045.4A| EP3287510B1|2014-11-04|2015-10-29|Method for hydrothermal carbonisation of biomass, and related device|
    PCT/IB2015/058360| WO2016071808A1|2014-11-04|2015-10-29|Method for the hydrothermal carbonisation of a biomass and associated device|
    AU2015341447A| AU2015341447B2|2014-11-04|2015-10-29|Method for the hydrothermal carbonisation of a biomass and associated device|
    US15/318,371| US10287505B2|2014-11-04|2015-10-29|Method for the hydrothermal carbonisation of a biomass and associated device|
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