• 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:
    In the solution shown, the sand to be cleaned is thermally cleaned by rotating the sand to be cleaned in a large furnace (1) by rotating the furnace (1). Pre-sand cleaning can be pre-treated by crushing the lumps and cleaning the sand fraction by magnetic separation. The rotating furnace is fed (5) pre-treated sand and thermal energy. The furnace (1) is set slightly inclined so that one end of the furnace (1) is lower than the first end. The incline and rotational speed of the furnace (1) and the amount of sand supplied are adjusted to adjust the speed of the sand and to maintain the ratio of the amount of sand in the cleaning to the volume of the furnace (1). The temperature of the furnace (1) is monitored from the coldest region of the furnace, which is substantially at the other end of the furnace. The temperature of the furnace (1) is adjusted by adjusting the amount of thermal energy to be supplied. By monitoring the temperature and knowing the speed of the sand, it is also possible to determine the average temperature of the sand and to adjust it by adjusting the desired thermal energy. Finally, the cleaned sand is drained (12) at one end of the furnace (1).
    公开号:FI20175944A1
    申请号:FI20175944
    申请日:2017-10-25
    公开日:2019-04-26
    发明作者:Toni Wesin；Timo Kronqvist
    申请人:Finn Recycling Oy；
    IPC主号:
    专利说明:

    Background of the Invention
    The invention relates to a method and apparatus for the thermal regeneration or purification of sand, foundry sand, used in a foundry.
    Prior art methods for the thermal recovery of the corresponding sand employ a so-called. fluidized bed boiler, in which a powerful air stream is fed upwards from the lower part of the furnace. The air stream causes the sand, ash and fuel used for heating to float.
    The problem with the arrangement described above is the slow process, high fuel cost and high loss per ton of refined sand. Imported sand is an alternative to cleaning. Imported sand is mainly imported from Central Europe. It has been collected from the bottom of the Atlantic and cleaned. As a matter of principle, imported sand must be imported at least to the detriment. Imported sand, or sand of sufficient quality that has already been used at least once in the foundry, is used15 for casting about 30% of the total amount of sand, since only mechanically recovered sand cannot be placed in direct contact with the cast due to impurities present. From an ecological point of view, it would be profitable to improve the purification process by reducing the need for imported sand and reducing the energy used for purification.
    Brief Description of the Invention
    It is therefore an object of the invention to provide a novel method and apparatus for carrying out the method, which is characterized by what is stated in the independent claims. Preferred embodiments of the invention are claimed in the dependent claims.
    In the solution shown, the sand to be cleaned is thermally cleaned by rotating the sand to be cleaned in a large, slightly sloping furnace by rotating the furnace. Before cleaning, sand can be pre-treated by crushing lumps and magnetic separation of the sand fraction. In the solution, the oven is set slightly inclined with one end of the oven lower than the first end of the en30. In the solution, mechanically pretreated cleanable sand and hot air, or thermal energy, are fed to the rotary kiln. The sand to be cleaned is fed into the furnace for cleaning preferably at the first end of the furnace. The furnace slope and rotation speed, as well as the sand feed rate, are controlled to adjust the sand propagation speed and keep the ratio of 35 sand to cleaning volume relative to the furnace volume desired. The oven temperature is monitored
    20175944 prh 25 -10-2017 is preferably tracked from the coldest region of the furnace substantially at the lower end of the furnace. The oven temperature is controlled by adjusting the amount of heat energy supplied. By monitoring the temperature and knowing the speed of the sand, it is also possible to determine the average temperature of the sand and adjust it by adjusting the desired heat energy supplied. Finally, the purified sand is drained from one end of the furnace.
    In the solution presented, sand cleaning is accelerated per tonne of sand to be cleaned and the sand is well cleaned and has a consistently high purity.
    According to one embodiment, the furnace temperature is controlled taking into account the purity of the sand to be cleaned, the composition of the dirt, or both.
    According to one embodiment, the furnace temperature is controlled taking into account the purity requirement of the purified sand.
    According to one embodiment, the furnace temperature is adjusted taking into account the amount of sand in the furnace.
    According to one embodiment, the furnace temperature is controlled by taking into account the speed of sand propagation in the furnace.
    According to one embodiment, the temperature of the furnace as measured by a temperature sensor located at one end of the furnace 20 is maintained at 400 to 900 degrees Celsius.
    According to one embodiment, the temperature of the furnace, as measured by a temperature sensor at one end of the furnace, is maintained at 550 to 750 degrees Celsius.
    According to one embodiment, the furnace slope and rotational speed are adjusted to achieve a purge time of 5 to 40 minutes for the sand, taking into account the purity of the sand to be cleaned.
    According to one embodiment, the sand to be cleaned preferably has a furnace through time of 10-30 minutes.
    According to one embodiment, the sand to be cleaned preferably has a furnace through time of 15 to 20 minutes.
    According to one embodiment, based on the composition of the sand to be cleaned as a precursor, after pre-treatment, after crushing and magnetic separation, the additive is added to the sand to be cleaned on the basis of the precursor by mixing the additive with sand.
    20175944 prh 25 -10- 2017
    BRIEF DESCRIPTION OF THE DRAWINGS
    The invention will now be further described in connection with preferred embodiments, with reference to the accompanying drawing:
    Figure 1 shows an embodiment of an apparatus for pretreatment and thermal recovery or purification of sand in an embodiment.
    DETAILED DESCRIPTION OF THE INVENTION
    Referring to the embodiment of Figure 1, the lumpy sand to be cleaned passes through pretreatment 2 to dispenser 3. Dispenser 3 feeds 10 sand to be cleaned to a conveyor 4 along which the sand is transferred to furnace 5 for cleaning. The sand is preferably fed into the furnace for cleaning, preferably from the first end 15 of the furnace. For example, when dropping from the dispenser 3 and moving through the conveyor 4, the sand can further be subjected to magnetic separation and dust removal.
    The furnace 1 is supplied with heat energy 6 produced by heat source 7. Preferably, the heat energy to be supplied is supplied to 6 furnaces at the first end of furnace 1. The thermal energy can be supplied elsewhere, for example at one end of the furnace 1 or in the middle region of the furnace 1. It is essential for the supply of thermal energy 6 and the transfer of sand 5 that the sand entering the furnace 5 is rapidly heated. The sand can be preheated outside the oven 1. Alternatively, the sand to be transferred to the furnace 1 may be preheated within the furnace 1, for example in a feed pipe which enters the furnace 1 preferably from the middle region of the furnace 1, Thermal energy can also be supplied to furnace 1 via 25 heat recovery systems at each site as deemed suitable. The heat source is, for example, a liquid gas burner 7. The furnace 1 is in the thermal insulation to reduce heat loss. The heat losses can be recovered and used, for example, to preheat the sand to be cleaned or to heat one or more properties. The furnace 1 is substantially supported by supports 20 30. Preferably, the supports 20 are provided with means for adjusting the inclination of the furnace. The slope adjustment arrangement may have been implemented in other ways, for example to tilt the entire apparatus. The most suitable solutions for adjusting the inclination of the furnace 1 can be adapted on a case-by-case basis. Most importantly, the inclination of the rotary furnace 1 can be adjusted. In addition, the apparatus includes means 35 for rotating and adjusting the rotation speed of the furnace 1.
    20175944 prh 25 -10- 2017
    At the other end 16 of the furnace 1, the flue gases 11 are removed, which also remove some of the dust brought by the sand. The flue gases also remove impurities from the sand. The flue gases are treated with appropriate filter arrangements 14 and cooled to recover heat. At one end 16 of the furnace 1, one or more temperature sensors 13 measure the temperature of the furnace and drain 12 thermally regenerated or purified sand from the furnace 1.
    The thermally recovered or purified sand may be discharged, for example, directly into a collector, container, tanker truck, open platform, sampling vessel, 10 for any other purpose, or via a conveyor or a conveyor, for example. If the sand is drained into an encapsulated conveyor, the encapsulated conveyor can further remove dust from the sand and the conveyor, or by any other suitable conveyor or transfer arrangement, may be further removed from the furnace for storage or disposal in suitable containers or transport equipment. It is essential that the foundry sand is reusable after it has been selected for each cleaning.
    When cleaning foundry sand, it usually contains such impurities, such as resin, which facilitate the combustion process. Therefore, the temperature of the furnace 1 must also be monitored when adjusting the amount of heat energy 6 supplied by the temperature sensors 13, for example when using the LPG burner 7, the conventional adjustments in the LPG burner 7 may prove to be more powerful due to impurities.
    One or more actuators of the apparatus are controlled by the control unit 40. The control unit 40 also monitors the values of the sensors and sensors in the equipment and utilizes the data to control the actuators. The control unit 40 may also be provided with different output data, advance information, as starting values. The control unit 40 is part of a control room connected to the equipment, from which the operation of the equipment 30 can be managed by various user interfaces. Various control room solutions are known per se and are therefore not further explained herein.
    The preliminary data measured and obtained from the sand to be cleaned is fed to the control unit 40. The control unit 40 takes these into account when determining the most appropriate parameters for the various actuators for the thermal recovery or purification of the batch of sand to be treated. Advance information can be given e.g. sand
    20175944 prh 25 -10- 2017 previous use, sand storage location (s) since previous use, moisture content of sand mass and sand temperature, for example as measured by one or more sensors in dispenser 3. Previous use indicates what impurities may be present in the sand due to previous use. The storage sites indicate what may have happened to the sand between the time of the previous use and the cleaning to be carried out. The temperature before cleaning, on the other hand, helps the control unit 40 determine the sand temperature through thermal regeneration or cleaning.
    In addition to the preliminary information, information is also required on the intended future use of the batch of sand or the desired purity of the purified sand. For example, a batch of sand can be regenerated back into foundry use, even so clean that it replaces some, if not all, virgin sand in the foundry. The virgin sand is therefore sand used as casting sand. Mechanically regenerated casting sand, or foundry sand, can be used in casting as filler 15 sand, but is not considered to be usable at all, or even as part of the casting sand.
    A lot of sand, or a part of it, can be cleaned a little lighter, for example, so that after cleaning it can no longer be classified as waste, but can be used for some other purpose. For example, the amount of sand still used in the foundry 20 is subject to limit values. Sand intended for other uses may be reduced or omitted to perform one or more dust removal steps if desired.
    In addition to monitoring the temperature of the furnace 1, the amount of sand to be fed to the furnace 1, its rate of passage in the furnace 1 and your cleaning, as well as the impurities in the sand being cleaned and how clean the sand is, are essential. As the propagation speed increases, the amount of heat energy supplied 6 must be increased. By increasing the rate of progression, essentially the same end result must be obtained by increasing the temperature of the furnace 1, which speeds up the thermal regeneration or purification. The higher the temperature of the furnace 1, there is a potential for greater heat loss, on the other hand, the throughput time is accelerated. At too high a temperature the sand starts to glaze. Thus, thermal regeneration or purification should be monitored using automation, which also means that various sensors, controls and gauges are needed and all, or at least most, of the automation is controlled by a control panel interface.
    20175944 prh 25 -10- 2017
    When cleaning foundry sand, there must be sufficient air space to remove impurities. The impurities are removed by the flue gases 11, so the amount of sand in the furnace 1 must be kept low enough. In other words, the sand-to-sand ratio should also be monitored. The higher the amount of sand in the furnace 1, the less impurities can escape from the sand with the flue gases. Therefore, in the case of sand to be recovered for foundry use, the sand content should be between 25% and 45% of the internal volume of the furnace. Preferably, the sand may be present in an amount of about 30-35% of the internal volume of furnace 1. It is also essential for determining the amount of sand and the rotational speed of the furnace 1 that the sand mass must not merely flow 10 along the bottom of the furnace 1, which means that the rotational speed is too low in relation to the amount of sand being cleaned. If the rotation speed of the furnace 1 is too high, the sand will rotate around the circumference of the furnace 1 with the furnace 1. With respect to the sand mass to be cleaned at a suitable rotation speed, the sand rises up to the edge of the furnace 1 so that at some point the sand mass detaches from the edge of the furnace 15 and at least partially falls in the air. In this case, the sand mass is thermally recovered or cleaned more uniformly because the sand mass is better mixed with the cleaning hot air, i.e. the sand to be cleaned appears and impurities are better removed with the air.
    Purified sand can be drained to a conveyor, collection container, transport container, dust extraction, or other suitable location, such as heat recovery prior to transportation or storage. Heat recovery can also be achieved from purified sand waiting to be transported or stored.
    According to one embodiment, after the magnetic separation, the additive is added to the pretreated sand to improve the purification of some specified impurities during thermal recovery. The additives used must be mixed very evenly with the sand to be cleaned. For this purpose, mixers have been designed which are known per se and are therefore not further described herein. Mixing is an important end result for kan30. The concentration of the additive should be uniform throughout the sand mass to be cleaned. Recommended concentrations, for example, with kaolin-based additives are in the order of 1-3% for fluidized bed boilers, but using the method and apparatus of the invention, it has been found that similar end results . In other words, the method and apparatus of the invention are so superior that it is known in the art
    20175944 prh 25 -10- 2017 needs 1-3% additive, similar results can be achieved even without additive. The dosing of the additive is influenced by the preliminary data measured and obtained from the sand to be cleaned.
    According to one embodiment, the temperature of the furnace 1 is controlled taking into account the average temperature of the sand to be cleaned.
    According to one embodiment, the temperature of the furnace 1 is substantially controlled taking into account the average sand temperature at one end of the furnace.
    The average sand temperature does not need to be measured directly from the sand being cleaned, as it can be calculated in many different ways. For example, the following data from the sensors and actuators on the control unit can be used to determine the average sand temperature: 1) the temperature of the furnace 1 at each time point, 2) the amount of sand being fed to each sand, , 5) the temperature of the 12 sand discharged, 6) the amount of heat energy 6 supplied at each time point, 7) the heat loss in the various parts of the plant, and 8) the temperature of the exhaust gas 11 discharged.
    According to one embodiment, the control unit 40 uses the information it obtains for each time point on furnace temperature, amount of 5 sand fed to furnace 1, rate of sand propagation, purity of purified sand, temperature of 5 and for controlling and adjusting the exhaust gas temperature and any other measured values as return data.
    Thus, the control unit 40 is able to make corrective control measures, for example in the control room, by means of the return information to achieve the target settings given to the control unit 40. Target values for, for example, the average sand temperature, the purified drained 12 sand, the exhaust 11 exhaust gas, or any combination of these, can be determined from the control room. Even at the rate of sand propagation, a target can be set and the actual values obtained as feedback data can be set by the control unit 40 to determine whether the target has been achieved and to make the necessary changes if the actual value calculated from the feedback data does not match the target.
    It will be obvious to a person skilled in the art that as technology advances, the basic idea of the invention can be implemented in many different ways. The invention and its embodiments are thus not limited to the examples described above, but may vary within the scope of the claims.
    权利要求:
    Claims (12)
    [1]
    The claims
    1. A method for cleaning sand used in a foundry, comprising pretreating lumps of sand to be cleaned by crushing the lumps into a sand fraction and purifying the sand fraction by magnetic separation.
    5 n e 11 u that:
    feeding (5) the pretreated sand to a rotary kiln (1);
    supplying (6) thermal energy to the rotary furnace (1);
    monitoring the temperature of the furnace (1) with one or more temperature sensors (13);
    Adjusting the temperature of the furnace (1) at least partially based on the temperature of the furnace being monitored by adjusting the amount of heat energy supplied (6);
    adjusting the amount of sand feed (5);
    adjusting the slope and rotation speed of the furnace (1) to adjust, at least in part, the amount of sand in the furnace (1) based on the amount of sand fed or the temperature of the furnace (1) or both and draining (12) purified sand at one end
    [2]
    Method according to claim 1, characterized in that the furnace (1) is heated by at least supplying thermal energy (6) to the furnace (1) at the first end (15) of the furnace (1).
    20
    [3]
    Method according to claim 1 or 2, characterized in that the pretreated sand is fed to the furnace (1) for cleaning at the first end of the furnace (1).
    [4]
    Method according to one of the preceding claims, characterized in that the temperature of the furnace (1) is adjusted taking into account the purity of the sand to be purified.
    20175944 prh 25 -10- 2017
    5. Something previous claims adequate method, known the fact that the temperature of the furnace (1) is adjusted to the amount of sand in the oven (1).6. Something previous claims adequate method,
    30 characterized in that the temperature of the furnace (1) is controlled taking into account the speed of the sand.
    Method according to one of the preceding claims, characterized in that the temperature of the furnace (1) is controlled taking into account the average temperature of the sand.
    Method according to one of the preceding claims, characterized in that the amount of sand in relation to the volume of the furnace (1) is maintained.
    20175944 prh 25 -10- 2017 essentially the same when cleaning sand of substantially similar purity.
    Method according to one of the preceding claims, characterized in that the sand to be purified is phenolic resin sand, furan resin.
    [5]
    5 sieve sand or pentonite resin sand.
    [6]
    The method according to any one of the preceding claims, characterized in that the method further comprises, after crushing and magnetic separation of the pre-treated cleaning sand, the composition of the pre-cleaning cleaning sand,
    10 on the basis of the additive to the sand to be cleaned by mixing the additive with a sand mixer.
    [7]
    Process according to Claim 10, characterized in that the additive is 0-0.3%.
    [8]
    A method according to any one of the preceding claims,
    15, characterized in that the temperature of the furnace (1) as measured by the temperature sensor (13) at one end (16) of the furnace (1) is between 400 and 900 degrees Celsius.
    [9]
    Method according to one of the preceding claims, characterized in that the temperature of the furnace (1), measured with the temperature sensor (13) located at one end of the furnace (16), is between 550 and 750 degrees Celsius.
    20
    [10]
    Apparatus for cleaning sand used in a foundry, characterized in that the apparatus comprises at least a rotary furnace (1) having means for adjusting the inclination and rotational speed of the furnace (1);
    a feeding device (4) having means for dispensing (5) the sand (1) to be cleaned;
    a heating arrangement having at least one or more temperature sensors (13) and one or more heat sources (7);
    means for removing purified sand from the furnace (1) at one end of the furnace (1); and
    A control unit for monitoring at least the information transmitted by one or more sensors in the apparatus and for controlling one or more actuators using the aforementioned monitored information transmitted by one or more sensors.
    [11]
    15. A computer program product, characterized in that it comprises
    35, and the program code means arranged to perform the steps of any of the methods defined in claims 1-10 when said computer program is executed on a computer.
    [12]
    A computer readable storage medium on which a computer program is recorded, characterized in that the computer program comprises program code means which causes the computer to perform the steps of any of the methods defined in claim 110 when said computer program is executed on a computer.
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    同族专利:
    公开号 | 公开日
    CN111316056A|2020-06-19|
    WO2019081815A1|2019-05-02|
    EP3701208A4|2021-09-01|
    US20200333074A1|2020-10-22|
    EP3701208A1|2020-09-02|
    FI128118B|2019-10-15|
    引用文献:
    公开号 | 申请日 | 公开日 | 申请人 | 专利标题
    US4941822A|1989-07-20|1990-07-17|Marvin Evans|Apparatus for heat treating contaminated particulate material|
    US5619936A|1993-05-28|1997-04-15|Kleen Soil Technologies, L.C.|Thermal desorption unit and processes|
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    EP3041624B1|2013-09-06|2018-12-12|Disa Industries A/S|Method of operating a metal foundry, system for performing the method, and metal foundry comprising the system|
    CN203956000U|2014-05-08|2014-11-26|中机中联工程有限公司|A kind of flue gas heat recovery system of sand regenerative system|
    CN104043772A|2014-06-20|2014-09-17|中机中联工程有限公司|Casting used sand thermal reclamation system|
    BR112017001787A2|2014-08-29|2018-07-17|Sintokogio Ltd|foundry sand conditioning system|
    WO2017090258A1|2015-11-27|2017-06-01|株式会社 松下工業|Core sand regeneration apparatus|
    法律状态:
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    优先权:
    申请号 | 申请日 | 专利标题
    FI20175944A|FI128118B|2017-10-25|2017-10-25|Thermal recovery or cleaning of sand|FI20175944A| FI128118B|2017-10-25|2017-10-25|Thermal recovery or cleaning of sand|
    EP18869873.2A| EP3701208A4|2017-10-25|2018-10-23|Thermal recovery or cleaning of sand|
    PCT/FI2018/050776| WO2019081815A1|2017-10-25|2018-10-23|Thermal recovery or cleaning of sand|
    CN201880069570.2A| CN111316056A|2017-10-25|2018-10-23|Heat recovery or purification of sand|
    US16/759,045| US20200333074A1|2017-10-25|2018-10-23|Thermal recovery or cleaning of sand|
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