Production of liquid fuels (sylvan liquid fuels) from 2-methylfuran

The present invention describes a procedure for the production of liquid fuel having a content high in alkanes and low in oxygenated compounds, comprising as a minimum: - a first step of alkylation of 2-methylfuran (commonly denominated Sylvan) with a furan alcohol 2 having the formula: (2), wherein R1 is H or an aliphatic or aromatic or heteroaromatic moiety, R2 is H or an aliphatic or aromatic or heteroaromatic moiety, and R3 isH, hydroxymethyl or an aliphatic or aromatic or heteroaromatic moiety, in the presence of a catalyst, - a second step of hydrogenation and dehydration of the compound obtained in step 1 in the presence of hydrogen, utilising suitable hydrogenation and dehydration catalysts.

Biofuel product and method for the production thereof

The invention relates to a method for producing a biofuel from an aqueous mixture of carbonized biomass obtained by means of a method for the hydrothermal carbonization of biomass, characterized in that it comprises: (a) grinding the aqueous mixture of carbonized biomass until a maximum size of less than 500 micrometers of the particles contained in the mixture is obtained; (b) applying a method for the physical separation of inorganic substances; and (c) reducing the moisture content until a water content of between 25 and 55 wt. % is reached. The invention also relates to the biofuel obtained by said method, and to the use thereof in various applications.

Method for converting biomass into liquid fuel

The invention relates to a method for producing liquid fuel having a high alkane content and a low oxygenized compound content, said method comprising at least: a first step of treating 2-methylfuran with a catalyst and water in reaction conditions in order to form a mixture of products with at least ten carbon atoms; and a second step of catalytic hydrogenation and dehydration of the product or the mixture obtained in step 1, using suitable hydrogenation and dehydration catalysts.

Method for extracting biochemical products obtained from a process of hydrothermal carbonization of biomass

The invention relates to a method for extracting biochemical products obtained from a process of hydrothermal carbonization of biomass, which includes feeding an aqueous mixture of biomass from a preheating tube for the aqueous mixture of biomass to a vertical reactor with a predetermined level of floatation and an area for accumulation of steam and gases in the upper part thereof, wherein said method for extracting biochemical products is characterized in that it includes (a) heating the aqueous mixture of biomass to, or above, evaporation temperature in said vertical reactor and/or in a previous stage of preheating the aqueous mixture of biomass, increasing the generation of stream and/or gases at the predetermined flotation level of the vertical reactor, (b) extracting the steam and/or gases generated in the previous stage and accumulated in the upper part of the vertical reactor, and (c) cooling the gases and/or condensing the steam extracted in the previous stage at different levels of temperature and pressure. The invention likewise relates to the biochemical product obtainable from said method, as well as to a system for implementing said method.

Method for converting biomass into liquid fuel

The invention relates to a method for producing liquid fuel having a high alkane content and a low oxygenised compound content, said method comprising at least: a first step of treating 2-methylfurane with a catalyst and water in reaction conditions in order to form a mixture of products with at least ten carbon atoms; and a second step of catalytic hydrogenation and dehydration of the product or the mixture obtained in step1, using suitable hydrogenation and dehydration catalysts.

Production of myrtanal from beta-pinene epoxide

The present invention relates to a procedure for the production of myrtanal from ss-pinene epoxide, comprising as a minimum putting said epoxide in contact with a crystalline microporous catalyst having pores of diameter of at least 0.52 nm and having an empirical formula in dehydrated calcined form of Hw(MwTixSnyZrzSi1-w-x-and-z)O2, where M is at least one metal of valency +3 selected from among Al, B, Ga, Fe, Cr, and combinations thereof; w is a molar fraction of M having a value between 0 and 2(x+y+z); x is a molar fraction of titanium having a value between 0 and 0.06; y is a molar fraction of tin having a value between 0 and 0.06; z is a molar fraction of zirconium having a value between 0 and 0.064, and wherein at least one of the three values "x", "y" or "z" differs from zero. In the present invention it is preferable for the crystalline microporous catalyst to have pores of at least 0.52 nm and a crystalline structure having an x-ray diffractogram corresponding to a beta zeolite ...

Production of liquid fuels (sylvan-liquid-fuels) from 2-methylfuran

The present invention describes a procedure for the production of liquid fuel having a content high in alkanes and low in oxygenated compounds, comprising as a minimum: —a first step of alkylation of 2-methylfuran (commonly denominated Sylvan) with a furan alcohol 2 having the formula: (2), wherein R 1 is H or an aliphatic or aromatic or heteroaromatic moiety, R 2 is H or an aliphatic or aromatic or heteroaromatic moiety, and R 3 is H, hydroxymethyl or an aliphatic or aromatic or heteroaromatic moiety, in the presence of a catalyst, —a second step of hydrogenation and dehydration of the compound obtained in step 1 in the presence of hydrogen, utilising suitable hydrogenation and dehydration catalysts.

METHOD FOR CONVERTING BIOMASS INTO LIQUID FUEL

The invention relates to a method for producing liquid fuel having a high alkane content and a low oxygenized compound content, said method comprising at least: a first step of treating 2-methylfurane with a catalyst and water in reaction conditions in order to form a mixture of products with at least ten carbon atoms; and a second step of catalytic hydrogenation and dehydration of the product or the mixture obtained in step 1, using suitable hydrogenation and dehydration catalysts. 1. A method for producing fuel characterized in that it comprises at least:a) A first step of treating 2-methylfurane with a catalyst and water in reaction conditions in order to form a mixture of products with at least ten carbon atoms.b) A second step of catalytic hydrogenation and dehydration of the mixture of products obtained in a).2. A method according to claim 1 , characterized in that in the first step a mixture of oxygenated hydrocarbons is formed.3. A method according to claim 1 , characterized in that in the first step the mixture of products comprises claim 1 , at least claim 1 , one oligomer of 2-methylfurane.4. A method according to claim 3 , characterized in that the oligomer obtained is present in a percentage of at least 20% by weight.5. A method according to claim 1 , characterized in that the products of the first step contain at least 15 carbon atoms.6. A method according to claim 1 , characterized in that the first step is carried out in the presence of an acid catalyst.7. A method according to claim 6 , characterized in that the first step is carried out in the presence of a mineral acid.8. A method according to claim 7 , characterized in that the first step is carried out in the presence of sulfuric acid.9. A method according to claim 6 , characterized in that the step 1 is carried out in the presence of an insoluble acid.10. A method according to claim 6 , characterized in that the step 1 is carried out in the presence of an acid resin.11. A method according to ...

Electric drive motor for a work apparatus

An electric drive motor for a work apparatus includes a stator having two stator poles which are at a distance from one another in the circumferential direction and have respective field windings. The motor has a rotor which rotates between the stator poles and the rotor shaft of the rotor drives a fan wheel. The cooling-air flow generated by the fan wheel enters the stator, flows therethrough and is discharged therefrom. For effective cooling, a pole intermediate space is provided between the stator poles; and, for the cooling-air flow, this space is filled by a non-magnetic guide body to provide a cooling duct delimited by the guide body and the field windings. The guide body is fastened to a support at one stator end and is inserted axially into the stator at the other end thereof.

METHOD FOR EXTRACTING BIOCHEMICAL PRODUCTS OBTAINED FROM A PROCESS OF HYDROTHERMAL CARBONIZATION OF BIOMASS

The invention relates to a method for extracting biochemical products obtained from a process of hydrothermal carbonization of biomass, which includes feeding an aqueous mixture of biomass from a preheating tube for the aqueous mixture of biomass to a vertical reactor with a predetermined level of floatation and an area for accumulation of steam and gases in the upper part thereof, wherein said method for extracting biochemical products is characterized in that it includes (a) heating the aqueous mixture of biomass to, or above, evaporation temperature in said vertical reactor and/or in a previous stage of preheating the aqueous mixture of biomass, increasing the generation of stream and/or gases at the predetermined flotation level of the vertical reactor, (b) extracting the steam and/or gases generated in the previous stage and accumulated in the upper part of the vertical reactor, and (c) cooling the gases and/or condensing the steam extracted in the previous stage at different levels of temperature and pressure. The invention likewise relates to the biochemical product obtainable from said method, as well as to a system for implementing said method. 1. Method for extracting biochemical products during a process of hydrothermal carbonization of biomass , comprising feeding an aqueous mixture of biomass from a preheating tube of the aqueous mixture of biomass to a vertical reactor with a defined level of flotation and an area for the accumulation of steam and gases in its upper portion , where said method for extracting biochemical products is characterized in that it comprises:(a) Heating the aqueous mixture of biomass up to or over the evaporation temperature in the same vertical reactor and/or in a prior preheating stage of the aqueous biomass mixture, increasing the generation of steam and/or gases at the set level of floatation of the vertical reactor.(b) Extracting the biochemicals alongside the steam and/or gasses generated in the previous stage, which ...

BIOFUEL PRODUCT AND METHOD FOR THE PRODUCTION THEREOF

The invention relates to a method for producing a biofuel from an aqueous mixture of carbonised biomass obtained by means of a method for the hydrothermal carbonisation of biomass, characterised in that it comprises: (a) grinding the aqueous mixture of carbonised biomass until a maximum size of less than 500 micrometres of the particles contained in the mixture is obtained; (b) applying a method for the physical separation of inorganic substances; and (c) reducing the moisture content until a water content of between 25 and 55 wt. % is reached. The invention also relates to the biofuel obtained by said method, and to the use thereof in various applications. 110-. (canceled)11. Process for obtaining a biofuel from an aqueous mixture of carbonised biomass obtained in a process for hydrothermal carbonisation of the biomass , characterised in that it comprises:(a) grinding the aqueous mixture of carbonised biomass, wherein the mixture has a carbon content of at least 60% and a content of volatile substances of between 50 and 70%, percentages which are expressed on a dry base and without ashes, until a maximum size of particles of less than 500 micrometers contained in the mixture is obtained;(b) applying a process for the physical separation of inorganic substances;(c) reducing the moisture content until a water content of between 25 and 55 wt. % is reached.12. Process according to claim 11 , characterised in that it comprises a pre-treatment to the aqueous mixture of carbonised biomass claim 11 , wherein said pre-treatment in turn comprises:(a) a first grinding of the aqueous mixture of carbonised biomass until a mean size of less than 5 mm of particles is obtained;(b) a first separation of inorganic substances;(c) a first dehydration step until a water content of less than 50 wt. %. is obtained.13. Process according to claim 11 , characterised in that it comprises an additional step of mixing and metering in at least one chemical dispersant in a percentage less than 3 ...

Composition and method for bleaching a substrate

PROCEDURE FOR THE EXTRACTION OF BIOCHEMICAL PRODUCTS OBTAINED FROM A BIOMASS HYDROTERMAL CARBONIZATION PROCESS.

Procedimiento para la extracción de productos bioquímicos obtenidos a partir de un proceso de carbonización hidrotermal de biomasa.#Es un primer objeto de esta invención un procedimiento para la extracción de productos bioquímicos obtenidos a partir de un proceso de carbonización hidrotermal de biomasa que comprende alimentar una mezcla acuosa de biomasa desde un tubo de precalentamiento de la mezcla acuosa de biomasa a un reactor vertical con un nivel de flotación definido y una zona de acumulación de vapores y gases en su parte superior, donde dicho procedimiento de extracción de productos bioquímicos se caracteriza porque comprende: (a) calentar hasta o por encima de la temperatura de evaporación de la mezcla acuosa de biomasa en el mismo reactor vertical y/o en una etapa anterior de precalentamiento de la mezcla acuosa de biomasa, incrementando la generación de vapores y/o gases en el nivel de flotación definido del reactor vertical; (b)extraer los vapores y/o gases generados en la etapa anterior y acumulados en la parte superior del reactor vertical; y (c) enfriar los gases y/o condensar los vapores extraídos en la etapa anterior a diferentes niveles de temperatura y presión. Asimismo, es objeto de la invención el producto bioquímico obtenible a partir de dicho procedimiento, así como el sistema para llevarlo a cabo. Procedure for the extraction of biochemical products obtained from a process of hydrothermal carbonization of biomass. # It is a first object of this invention a procedure for the extraction of biochemical products obtained from a process of hydrothermal carbonization of biomass comprising feeding a aqueous mixture of biomass from a preheating tube of the aqueous mixture of biomass to a vertical reactor with a defined flotation level and a zone of accumulation of vapors and gases in its upper part, where said biochemical product extraction process is characterized in that It comprises: (a) heating up to or above the evaporation temperature of the ...

BIOFUEL PRODUCT AND OBTAINING PROCESS

Producto biocombustible y proceso de obtención.#La presente invención se refiere a un proceso para la obtención de un biocombustible a partir de una mezcla acuosa de biomasa carbonizada obtenida en un proceso de carbonización hidrotermal de biomasa, caracterizado porque comprende: (a) moler la mezcla acuosa de biomasa carbonizada hasta obtener un tamaño máximo de las partículas contenidas en la mezcla inferior a 500 micrómetros; (b) aplicar un proceso de separación física de inorgánicos; y (c) reducir el contenido de humedad hasta alcanzar un contenido de agua comprendido entre un 25% y un 55% en peso. Es asimismo objeto de la invención el biocombustible obtenido a partir de dicho proceso, así como su uso en distintas aplicaciones. Biofuel product and process for obtaining. # The present invention relates to a process for obtaining a biofuel from an aqueous mixture of carbonized biomass obtained in a process of hydrothermal carbonization of biomass, characterized in that it comprises: (a) grinding the aqueous mixture of carbonized biomass to obtain a maximum size of the particles contained in the mixture of less than 500 micrometers; (b) apply a physical inorganic separation process; and (c) reduce the moisture content until reaching a water content between 25% and 55% by weight. The object of the invention is also the biofuel obtained from said process, as well as its use in different applications.

Renewable carbonaceous material and process for its production from biomass (Machine-translation by Google Translate, not legally binding)

Renewable carbonaceous material and process for its production from biomass. The present invention relates to a value-added renewable carbonaceous material, a process for obtaining it by hydrothermal carbonization from lignocellulosic biomass with an amount of water comprised between 50% and 90% by weight, and its use as a substrate or additive without phytotoxic effect for the soil in agricultural plantations or as solid fuel. (Machine-translation by Google Translate, not legally binding)

Method for extracting biochemical products obtained from a process of hydrothermal carbonization of biomass

The invention relates to a method for extracting biochemical products obtained from a process of hydrothermal carbonization of biomass, which includes feeding an aqueous mixture of biomass from a preheating tube for the aqueous mixture of biomass to a vertical reactor with a predetermined level of floatation and an area for accumulation of steam and gases in the upper part thereof, wherein said method for extracting biochemical products is characterized in that it includes: (a) heating the aqueous mixture of biomass to, or above, evaporation temperature in said vertical reactor and/or in a previous stage of preheating the aqueous mixture of biomass, increasing the generation of steam and/or gases at the predetermined flotation level of the vertical reactor; (b) extracting the steam and/or gases generated in the previous stage and accumulated in the upper part of the vertical reactor; and (c) cooling the gases and/or condensing the steam extracted in the previous stage at different levels of temperature and pressure. The invention likewise relates to the biochemical product obtainable from said method, as well as to a system for implementing said method.

Method for extracting biochemical products obtained from a process of hydrothermal carbonization of biomass

The present invention relates to a method for extracting biochemical products obtained from a process of hydrothermal carbonization of biomass, which includes feeding an aqueous mixture of biomass from a preheating tube for the aqueous mixture of biomass to a vertical reactor with a predetermined level of floatation and an area for accumulation of steam and gases in the upper part thereof, wherein said method for extracting biochemical products is characterized in that it includes (a) heating the aqueous mixture of biomass to, or above, evaporation temperature in said vertical reactor and/or in a previous stage of preheating the aqueous mixture of biomass, increasing the generation of stream and/or gases at the predetermined flotation level of the vertical reactor, (b) extracting the steam and/or gases generated in the previous stage and accumulated in the upper part of the vertical reactor, and (c) cooling the gases and/or condensing the steam extracted in the previous stage at different levels of temperature and pressure. The invention likewise relates to the biochemical product obtainable from said method, as well as to a system for implementing said method.

Manually operated work device

Ein handgeführtes Arbeitsgerät besitzt mindestens ein Werkzeug, das von einem Motor (21) angetrieben ist. Das Arbeitsgerät besitzt einen Akku (6) zum Antrieb des Werkzeugs und ein Führungsrohr (3). An einem ersten Ende (4) des Führungsrohrs (3) ist der Akku (6) angeordnet und an einem zweiten Ende (5) der Motor (21) und das Werkzeug. Der Luftaustrittsspalt (35) aus dem Motorgehäuse (12) ist vorteilhaft ringförmig ausgebildet. In den Luftaustrittsspalt (35) ragt mindestens eine Leitschaufel (38). Der Motor (21) ist im Motorgehäuse (12) derart elastisch gelagert, dass er bei am Werkzeug eingeleiteten Querkräften (F) im Motorgehäuse (12) kippen kann. A hand-held implement has at least one tool driven by a motor (21). The implement has a battery (6) for driving the tool and a guide tube (3). At a first end (4) of the guide tube (3), the battery (6) is arranged and at a second end (5) of the motor (21) and the tool. The air outlet gap (35) from the motor housing (12) is advantageously annular. In the air outlet gap (35) protrudes at least one vane (38). The motor (21) is mounted elastically in the motor housing (12) in such a way that it can tilt in the motor housing (12) when the transverse forces (F) introduced at the tool are present.

METHOD FOR EXTRACTING BIOCHEMICAL PRODUCTS OBTAINED FROM A BIOMASS HYDROTHEROMIC CARBONIZATION PROCESS

resumo método para extrair produtos bioquímicos obtidos a partir de um processo de carbonização hidrotérmica de biomassa a presente invenção refere-se a um método para extrair produtos bioquímicos obtidos a partir de um 5 processo de carbonização hidrotérmica de biomassa, que inclui alimentar uma mistura aquosa de biomassa a partir de um tubo de preaquecimento para a mistura aquosa de biomassa para um reator vertical com um nível predeterminado de flotação e uma área para o acúmulo de vapor e gases na sua 10 parte superior, em que o dito método para extração de produtos bioquímicos é caracterizado pelo fato de incluir (a) aquecimento da mistura aquosa de biomassa para, ou acima de, a temperatura de evaporação no dito reator vertical e/ou em uma etapa anterior de preaquecimento da 15 mistura aquosa de biomassa, aumentar a geração de vapor e/ou gases sob o nível de flotação predeterminado do reator vertical, (b) extrair o vapor e/ou gases gerados na etapa anterior e acumulados na parte superior do reator vertical, e (c) resfriar os gases e/ou condensar o vapor 20 extraído na etapa anterior sob diferentes níveis de temperatura e pressão. de forma assemelhada, a invenção refere-se ao produto bioquímico suscetível de ser obtido a partir do referido método, bem como a um sistema para a realização do referido método. 25 Abstract Method for extracting biochemicals obtained from a hydrothermal biomass carbonization process The present invention relates to a method for extracting biochemicals obtained from a hydrothermal biomass carbonization process, which includes feeding an aqueous mixture of biomass from a preheat tube for the aqueous biomass mixture to a vertical reactor with a predetermined flotation level and an area for vapor and gas accumulation at its top 10, wherein said method for extracting biochemicals is characterized by including (a) heating the aqueous biomass mixture to or above the evaporation temperature in said vertical reactor and / or in an earlier ...

Method for the extraction of biochemical products obtained from a biomass hydrothermal carbonization process

La presente invención se refiere a un procedimiento para la extracción de productos bioquímicos obtenidos a partir de un proceso de carbonización hidrotermal de biomasa que comprende alimentar una mezcla acuosa de biomasa desde un tubo de precalentamiento de la mezcla acuosa de biomasa a un reactor vertical con un nivel de flotación definido y una zona de acumulación de vapores y gases en su parte superior, donde dicho procedimiento de extracción de productos bioquímicos se caracteriza por que comprende: (a) calentar hasta o por encima de la temperatura de evaporación de la mezcla acuosa de biomasa en el mismo reactor vertical y/o en una etapa anterior de precalentamiento de la mezcla acuosa de biomasa, incrementando la generación de vapores y/o gases en el nivel de flotación definido del reactor vertical; (b) extraer los vapores y/o gases generados en la etapa anterior y acumulados en la parte superior del reactor vertical; y (c) enfriar los gases y/o condensar los vapores extraídos en la etapa anterior a diferentes niveles de temperatura y presión. Así mismo es objeto de la invención el producto bioquímico obtenible a partir de dicho procedimiento, así como el sistema para llevarlo a cabo. The present invention relates to a process for the extraction of biochemical products obtained from a biomass hydrothermal carbonization process comprising feeding an aqueous mixture of biomass from a preheating tube of the aqueous biomass mixture to a vertical reactor with a vertical defined flotation level and a zone of accumulation of vapors and gases in its upper part, where said biochemical product extraction process is characterized by comprising: (a) heating up to or above the evaporation temperature of the aqueous mixture of biomass in the same vertical reactor and / or in an earlier stage of preheating the aqueous biomass mixture, increasing the generation of vapors and / or gases at the defined flotation level of the vertical reactor; (b) extract the vapors and / or ...

Electric drive motor for a work apparatus

An electric drive motor for a work apparatus includes a stator having two stator poles which are at a distance from one another in the circumferential direction and have respective field windings. The motor has a rotor which rotates between the stator poles and the rotor shaft of the rotor drives a fan wheel. The cooling-air flow generated by the fan wheel enters the stator, flows therethrough and is discharged therefrom. For effective cooling, a pole intermediate space is provided between the stator poles; and, for the cooling-air flow, this space is filled by a non-magnetic guide body to provide a cooling duct delimited by the guide body and the field windings. The guide body is fastened to a support at one stator end and is inserted axially into the stator at the other end thereof.

Biofuel product and method for the production thereof

"Electric drive motor for a working device"

Elektrischer Antriebsmotor für ein Arbeitsgerät, bestehend aus einem Stator (4) mit mindestens zwei Statorpolen (30), die in Umfangsrichtung mit Abstand zueinander liegen und jeweils eine elektrische Erregerwicklung (32) tragen, sowie mit einem zwischen den Statorpolen (30) drehenden Rotor (10), dessen Rotorwelle (9) ein Lüfterrad (20) antreibt, wobei der vom Lüfterrad (20) erzeugte Kühlluftstrom (42) in den Stator (4) eintritt, den Stator (4) durchströmt und ausgeblasen wird. Zur Erzielung einer wirksamen Kühlung ist ein in Umfangsrichtung zwischen den Statorpolen (30) liegender Polzwischenraum (34) durch einen nicht magnetischen Leitkörper (61) derart gefüllt ist, dass ein durch den Leitkörper (61) und die Erregerwicklung (32) begrenzter Kühlkanal (40) für den Kühlluftstrom (42) ausgebildet ist, wobei der Leitkörper (61) an einem Ende an einem Träger (18) festliegt und mit dem anderen Ende axial in den Stator (4) eingeschoben ist. Electric drive motor for a working device, consisting of a stator (4) with at least two stator poles (30), which are spaced apart from one another in the circumferential direction and each carry an electrical excitation winding (32), and with a rotor rotating between the stator poles (30) 10), the rotor shaft (9) of which drives a fan wheel (20), the cooling air flow (42) generated by the fan wheel (20) entering the stator (4), the stator (4) flowing through and being blown out. To achieve effective cooling, a pole gap (34) lying in the circumferential direction between the stator poles (30) is filled by a non-magnetic guide body (61) in such a way that a cooling channel (40) delimited by the guide body (61) and the excitation winding (32) ) for the cooling air flow (42), the guide body (61) being fixed at one end to a support (18) and being axially inserted into the stator (4) at the other end.

Personnel lift with a traction sheave drive and a cabin

The lift has a traction-sheave drive constructed with nominal load according to EN 81-1, EN 81-2, where the load is reduced to a usable surface of a cabin. The drive has a controller connected with a sensor e.g. load weighing sensor and/or a movement direction detection sensor. The drive is shiftable and/or a brake is actuatable and/or contouring error monitoring of a frequency converter is triggered by the senor under evaluation of sensor signals. Load accommodating elements are made of metallic material e.g. steel spring.

Production of myrtanal from beta-pinene epoxide

The present invention relates to a procedure for the production of myrtanal from β-pinene epoxide, comprising as a minimum putting said epoxide in contact with a crystalline microporous catalyst having pores of diameter of at least 0.52 nm and having an empirical formula in dehydrated calcined form of H w (M w Ti x Sn y Zr z Si 1-w-x-and-z )O 2 , where M is at least one metal of valency +3 selected from among Al, B, Ga, Fe, Cr, and combinations thereof; w is a molar fraction of M having a value between 0 and 2(x+y+z); x is a molar fraction of titanium having a value between 0 and 0.06; y is a molar fraction of tin having a value between 0 and 0.06; z is a molar fraction of zirconium having a value between 0 and 0.064, and wherein at least one of the three values "x", "y" or "z" differs from zero. In the present invention it is preferable for the crystalline microporous catalyst to have pores of at least 0.52 nm and a crystalline structure having an x-ray diffractogram corresponding to a beta zeolite.

The oxidation of ketones to esters using a tin substituted zeolite beta

Biopolymers and obtaining process (Machine-translation by Google Translate, not legally binding)

The present invention belongs to the field of the chemical industry, more specifically to the field of the conversion of biomass to a solid polymeric product with added value. The invention provides a process for obtaining biopolymers in which the amount by weight corresponding to phenol has been replaced at least partially by a lower cost renewable residual material. This process is characterized in that it comprises a step of hydrothermal carbonization of lignocellulosic biomass, and the subsequent addition of a total amount of one or more phenolic compounds and a total amount of aldehyde, followed by heat treatment of the product obtained. (Machine-translation by Google Translate, not legally binding)

Hydrochar

The present invention relates to a value-added, renewable carbonaceous material, to a method for obtaining said material by means of hydrothermal carbonization from lignocellulosic biomass with an amount of water of between 50% and 90% by weight, and to the use of same as a solid fuel or as a substrate or additive without phytotoxic effects on agricultural soil.

Electric drive motor for a machine tool

Elektrischer Antriebsmotor für ein Arbeitsgerät, bestehend aus einem Stator (4) mit mindestens zwei Statorpolen (30), die in Umfangsrichtung mit Abstand zueinander liegen und jeweils eine elektrische Erregerwicklung (32) tragen, sowie mit einem zwischen den Statorpolen (30) drehenden Rotor (10), dessen Rotorwelle (9) ein Lüfterrad (20) antreibt, wobei der vom Lüfterrad (20) erzeugte Kühlluftstrom (42) in den Stator (4) eintritt, den Stator (4) durchströmt und ausgeblasen wird. Zur Erzielung einer wirksamen Kühlung ist ein in Umfangsrichtung zwischen den Statorpolen (30) liegender Polzwischenraum (34) durch einen nicht magnetischen Leitkörper (61) derart gefüllt ist, dass ein durch den Leitkörper (61) und die Erregerwicklung (32) begrenzter Kühlkanal (40) für den Kühlluftstrom (42) ausgebildet ist, wobei der Leitkörper (61) an einem Ende an einem Träger (18) festliegt und mit dem anderen Ende axial in den Stator (4) eingeschoben ist. Electric drive motor for a working device, comprising a stator (4) with at least two stator poles (30) which are spaced apart in the circumferential direction and each carry an electrical field winding (32), and with a rotating between the stator poles (30) rotor ( 10) whose rotor shaft (9) drives a fan wheel (20), wherein the cooling air flow (42) generated by the fan wheel (20) enters the stator (4), flows through the stator (4) and is blown out. To achieve effective cooling, a pole interspace (34) lying in the circumferential direction between the stator poles (30) is filled by a nonmagnetic guide body (61) such that a cooling channel (40) delimited by the guide body (61) and the field winding (32) ) is formed for the cooling air flow (42), wherein the guide body (61) at one end to a carrier (18) is fixed and is inserted axially into the stator (4) with the other end.

Production of liquid fuels (sylvan-liquid-fuels) from 2-methylfuran

The present invention describes a procedure for the production of liquid fuel having a content high in alkanes and low in oxygenated compounds, comprising as a minimum: a first step of alkylation of 2-methylfuran (commonly denominated Sylvan) with a furan alcohol 2 having the formula: (2), wherein R 1 is H or an aliphatic or aromatic or heteroaromatic moiety, R 2 is H or an aliphatic or aromatic or heteroaromatic moiety, and R 3 is H, hydroxymethyl or an aliphatic or aromatic or heteroaromatic moiety, in the presence of a catalyst, a second step of hydrogenation and dehydration of the compound obtained in step 1 in the presence of hydrogen, utilizing suitable hydrogenation and dehydration catalysts.

Method for converting biomass into liquid fuel

The invention relates to a method for producing liquid fuel having a high alkane content and a low oxygenized compound content, said method comprising at least: a first step of treating 2-methylfurane with a catalyst and water in reaction conditions in order to form a mixture of products with at least ten carbon atoms; and a second step of catalytic hydrogenation and dehydration of the product or the mixture obtained in step 1, using suitable hydrogenation and dehydration catalysts.

Biofuel product and method for the production thereof

The invention relates to a method for producing a biofuel from an aqueous mixture of carbonised biomass obtained by means of a method for the hydrothermal carbonisation of biomass, characterised in that it comprises: (a) grinding the aqueous mixture of carbonised biomass until a maximum size of less than 500 micrometres of the particles contained in the mixture is obtained; (b) applying a method for the physical separation of inorganic substances; and (c) reducing the moisture content until a water content of between 25 and 55 wt.% is reached. The invention also relates to the biofuel obtained by said method, and to the use thereof in various applications.

Biopolymers and obtaining process

La presente invención pertenece al campo de la industria química, más concretamente al campo de la conversión de biomasa a un producto sólido polimérico con valor añadido. La invención proporciona un procedimiento para la obtención de biopolímeros en los que se ha sustituido al menos parcialmente la cantidad en peso correspondiente al fenol por un material residual renovable de coste menor Dicho procedimiento está caracterizado porque comprende una etapa de carbonización hidrotermal de biomasa lignocelulósica, y la adición posterior de una cantidad total de uno o más compuestos fenólicos y una cantidad total de aldehído, seguida del tratamiento térmico del producto obtenido. The present invention belongs to the field of the chemical industry, more specifically to the field of the conversion of biomass to a polymeric solid product with added value. The invention provides a process for obtaining biopolymers in which at least partially the amount by weight corresponding to phenol has been replaced by a renewable waste material of lower cost. This process is characterized in that it comprises a stage of hydrothermal carbonization of lignocellulosic biomass, and the subsequent addition of a total amount of one or more phenolic compounds and a total amount of aldehyde, followed by heat treatment of the product obtained.

Aldehyde conversion method using a molecular sieve and the use of the molecular sieve as a catalyst in said method

Method and system for steamcracking

A method of steam cracking using a steam cracking using a steam cracking system (100) including a first steam cracking furnace unit (1000) or a plurality of first steam cracking furnace units (1000) and a second steam cracking furnace unit (2000) or a plurality of second steam cracking furnace units (2000) is proposed, wherein the first steam cracking furnace unit (1000) or each of the plurality of first steam cracking furnace units (1000) comprises one or more fired steam cracking furnaces (110), the second steam cracking furnace unit (2000) or each of the plurality of second steam cracking furnace units (2000) comprises one or more electric steam cracking furnaces (210), and the first steam cracking furnace unit (1000) or each of the plurality of first steam cracking furnace units (1000) comprises means for preheating at least a part of combustion air provided to its fired steam cracking furnace or furnaces (110) to a temperature level of at least 100 °C. A corresponding system (100) is also part of the present invention.

Method and system for steamcracking

A method of steam cracking using a steam cracking arrangement (2100-2800) including an electric cracking furnace (10) without a convection zone (12) and further including a quench cooling train (20) is proposed, wherein a process gas stream is passed at least through the electric cracking furnace (10) and the quench cooling train (20). It is provided that that the quench cooling train (20) is operated to comprise at least two distinct cooling steps arranged in either order, wherein in a first one of the cooling steps at least a part of the process gas stream withdrawn from the electric cracking furnace (10) is cooled against vaporizing boiler feed water at an absolute pressure level between 30 and 175 bar and wherein in a second one of the cooling steps at least a part of the process gas stream withdrawn from the electric cracking furnace (10) is cooled against a superheated mixture of feed hydrocarbons and process steam used in forming the process gas stream which is thereby heated to a temperature level between 350 and 750°C. A corresponding arrangement (2100-2800) is also part of the present invention.

Method and system for steam cracking

A method of steam cracking using a steam cracking system including one or more fired radiant sections is provided herein, wherein, during a steam cracking operation, a fuel is combusted with oxidizer gas to heat the one or more fired radiant sections, forming a flue gas, a process gas is formed using a hydrocarbon feed and process steam, and the process gas is passed through one or more coils in the one or more fired radiant sections, forming a cracked gas, wherein at least a part of the flue gas is cooled in a flue gas heat recovery section, wherein at least a part of the cracked gas is cooled in a cracked gas heat recovery section, wherein the flue gas heat recovery section and the cracked gas heat recovery section each comprise one or more multistream heat exchangers. The flue gas heat recovery section comprises heat exchange structures which are provided in an amount and a configuration such as to use, at least during a part of the steam cracking operation, a first proportion of more than 35% of a total amount of heat recovered within the one or more multistream heat exchangers of the flue gas heat recovery section from the flue gas for preheating at least a part of the oxidizer gas, and wherein the cracked gas heat recovery section is configured such as to use, at least during the same part of the steam cracking operation, a second proportion of more than 35% of a total amount of heat recovered within the one or more multistream heat exchangers of the cracked gas heat recovery section for preheating at least a part of the process gas and/or the hydrocarbon feed and/or the process steam. A corresponding system is also part of the present invention.

Hochdruckreinigungsgerät

Die Erfindung betrifft ein Hochdruckreinigungsgerät (1) umfassend einen Anschluss (2) für eine Flüssigkeitsquelle (14), eine Hochdruckpumpe (3), eine Hauptleitung (5), durch die mittels der Hochdruckpumpe (3) Flüssigkeit von dem Anschluss (2) zu einer Ausspritzöffnung (6) der Hauptleitung (5) förderbar ist, ein Hauptleitungsventil (8), das in der Hauptleitung (5) angeordnet ist und ein Bedienelement (7). Das Hauptleitungsventil (8) unterbindet in einem geschlossenen Zustand (20) einen Durchfluss von Flüssigkeit durch die Hauptleitung (5) und lässt in einem offenen Zustand (40) einen Durchfluss von Flüssigkeit durch die Hauptleitung (5) zu. Das Hauptleitungsventil (8) ist mittels des Bedienelements (7) zwischen dem offenen Zustand (20) und dem geschlossenen Zustand (40) schaltbar. Die Hauptleitung (5) weist zwischen dem Anschluss (2) und der Hochdruckpumpe (3) einen Saugraum (9) und zwischen der Hochdruckpumpe (3) und der Ausspritzöffnung (6) einen Druckraum (10) auf. Der Druckraum (10) ist mit dem Saugraum (9) fluidisch über eine Bypassleitung (12) verbunden. In der Bypassleitung (12) ist ein Bypassventil (13) angeordnet. Zur Regulierung des Drucks im Druckraum (10) mittels des Bypassventils (13) ist eine freie Querschnittsfläche der Bypassleitung (12) einstellbar. Das Bypassventil (13) ist zur Einstellung der freien Querschnittsfläche der Bypassleitung (12) mittels des Bedienelements (7) verstellbar.

Zusammensetzung und verfahren zum bleichen eines substrats

Elemento de retención y ensamblaje de agarre de material de construcción que comprende el mismo

Un elemento de sujeción (1; 1') con un cuerpo de lengüeta de un material FRP en forma de placa con una zona de fijación (2), en la que se puede fijar el cuerpo de lengüeta a un dispositivo de soporte (17) y una zona de sujeción (3). A través del cual se aplica una fuerza de sujeción al dispositivo a sujetar, se puede aplicar una zona de flexión (4) entre la zona de fijación (2) y la zona de sujeción (3), en la que el cuerpo de lengüeta es elásticamente deformable cuando la fuerza de sujeción se aplica al objeto a sujetar y un dispositivo de agarre (100) para plegar una capa de elementos de material de construcción con al menos un elemento de sujeción (1; 1') según la invención. (Traducción automática con Google Translate, sin valor legal)

Biopolymers and preparation method

Aldehyde conversion method using a molecular sieve and the use of the molecular sieve as a catalyst in said method

The inversion relates to an aldehyde conversion method comprising putting an aldehyde into contact with oxygenated water and with a catalyst, under oxidation conditions, wherein the catalyst is a molecular sieve with pores of a diameter of at least 0.52 nm and has an empirical formula in a calcined and dehydrated form of (Sn x Ti y Si 1−x−y−z Ge z ) O 2 wherein x is a molar fraction of the tin and has a value between 0.001 and 0.1; y is a molar fraction of titanium and has a value from zero to 0.1; and z is the molar fraction molar of the germanium and has a value from zero to 0.08.

Biopolymers and preparation method

Un procedimiento para la conversion de aldehidos usando un tamiz molecular y uso del tamiz molecular como catalizador en el procedimiento.

Un procedimiento para la conversión de aldehídos usando un tamiz molecular y uso del tamiz molecular como catalizador en el procedimiento. Un procedimiento para la conversión de aldehídos que comprende poner en contacto un aldehído con agua oxigenada y con un catalizador, en condiciones de oxidación, caracterizado porque el catalizador es un tamiz molecular con poros de un diámetro de al menos 0,52 mm y tiene una fórmula empírica en forma calcinada y deshidratada de (SnxTiySi1-x-y-zGez)O2 donde x es una fracción molar del estaño y tiene un valor entre 0,001 y 0,1; y es una fracción molar de titanio y tiene un valor de cero a 0,1; y z es la fracción molar del germanio y tiene un valor de cero a 0,08.

Halteelement und baustoffgreiferanordnung mit einem solchen

Method and System for Steamcracking

A method of steam cracking includes using a steam cracking arrangement that has a fired cracking furnace, a quench cooling train, and rotating equipment at least partly driven by electric energy. A process gas stream is passed through the furnace and the cooling train. A steam generation arrangement, operated in thermal association with the cracking arrangement, results in superheated high pressure steam at a first pressure level of 30 and 175 bar absolute pressure and at a first temperature level. No steam at a higher temperature level than the first is generated. The superheated high pressure steam is partially adiabatically and isenthalpically expanded to a second lower pressure level. The first temperature level is selected such that each intermediate temperature level reached at intermediate pressure levels of more than 20 bar during the adiabatic and isenthalpic expansion process is between 5 and 120 K above the dew point of steam.

Aufzugsanlage

Method and plant for steam cracking

The present invention relates to a method for converting one or more hydrocarbons by means of steam cracking, wherein one or more input streams (F) containing the one or more hydrocarbons (H) are led through one or more radiant zones (11) of one or more cracker furnaces (10), such that one or more product streams (C) are obtained; wherein the one or more radiant zones (11) are heated by the burning of heating gas (X) with combustion air (L); wherein at least part of the combustion air (L) is subjected to combustion air preheating (75); wherein steam (S, T) is produced from feed water (W); and wherein the feed water (W) is subjected to feed water preheating in one or more convection zones (12) of the one or more cracker furnaces (10). The combustion air preheating (75) is carried out, at least partly and/or at least some of the time, by the use of heat drawn from at least part of the feed water (W) upstream of the feed water preheating. The present invention also relates to a corresponding plant.

Método e planta para craqueamento a vapor

método e planta para craqueamento a vapor. a presente invenção refere-se a um método para reação de um ou mais hidrocarbonetos por craqueamento a vapor, no qual são conduzidas uma ou mais correntes de entrada (f) contendo um ou mais hidrocarbonetos (h), obtendo-se uma ou mais correntes de produto (c), através da uma ou mais zonas de radiação (11) do um ou mais fornos de craqueamento (10), nos quais uma ou mais zonas de radiação (11) são aquecidas pela queima de gás de aquecimento (x) com ar de combustão (l), em que pelo menos um porção do ar de combustão (l) é submetida ao pré-aquecimento do ar de combustão (75) no qual o vapor (s, t) é produzido a partir da água de alimentação (w), e no qual a água de alimentação (w) é submetida ao pré- aquecimento da água de alimentação em uma ou mais zonas de convecção (12) de um ou mais fornos de craqueamento (10). o pré-aquecimento do ar de combustão (75) é realizado pelo menos em parte e/ou pelo menos temporariamente usando o calor retirado de pelo menos parte da água de alimentação (w) a montante do pré-aquecimento de água de alimentação. a presente invenção também se refere a um sistema correspondente.

Method and plant for steam cracking

The present invention relates to a method for converting one or more hydrocarbons by means of steam cracking, wherein one or more input streams (F) containing the one or more hydrocarbons (H) are led through one or more radiant zones (11) of one or more cracker furnaces (10), such that one or more product streams (C) are obtained; wherein the one or more radiant zones (11) are heated by the burning of heating gas (X) with combustion air (L); wherein at least part of the combustion air (L) is subjected to combustion air preheating (75); wherein steam (S, T) is produced from feed water (W); and wherein the feed water (W) is subjected to feed water preheating in one or more convection zones (12) of the one or more cracker furnaces (10). The combustion air preheating (75) is carried out, at least partly and/or at least some of the time, by the use of heat drawn from at least part of the feed water (W) upstream of the feed water preheating. The present invention also relates to a corresponding plant.

Method and System for Steamcracking

A method of steam cracking using a steam cracking arrangement including an electric cracking furnace without a convection zone and a quench cooling train is proposed, wherein a process gas stream is passed through the cracking furnace and the cooling train. The cooling train is operated to comprise at least two distinct cooling steps arranged in either order, wherein in a first cooling step at least a part of the process gas stream withdrawn from the electric cracking furnace is cooled against vaporizing boiler feed water at an absolute pressure level between 30 and 175 bar and wherein in a second cooling step at least a part of the process gas stream withdrawn from the electric cracking furnace is cooled against a superheated mixture of feed hydrocarbons and process steam used in forming the process gas stream which is thereby heated to a temperature level between 350 and 750° C.

Method and System for Steamcracking

A method of steam cracking using a steam cracking system includes a first steam cracking furnace unit or a plurality of first steam cracking furnace units and a second steam cracking furnace unit or a plurality of second steam cracking furnace units. The first steam cracking furnace unit or each of the plurality of first steam cracking furnace units comprises one or more fired steam cracking furnaces. The second steam cracking furnace unit or each of the plurality of second steam cracking furnace units comprises one or more electric steam cracking furnaces. The first steam cracking furnace unit or each of the plurality of first steam cracking furnace units further includes means for preheating at least a part of combustion air provided to its fired steam cracking furnace or furnaces to a temperature level of at least 100° C.

Method and system for steamcracking

A method of steam cracking using a steam cracking arrangement (1100-1500) including one or more fired cracking furnaces (110), one or more quench cooling trains (20) and one or more compressors (60) and/or pumps as rotating equipment is proposed, wherein one or more process gas streams is or are passed at least through the one or more fired cracking furnaces (110) and the one or more quench cooling trains (20), and wherein the rotating equipment is at least partly driven by electric energy. According to the invention, one or more steam generation arrangements (30) is or are operated in thermal association with the one or more steam cracking arrangements (1100-1500), wherein using the one or more steam generation arrangements (30) at least superheated high pressure steam at a first pressure level of 30 and 175 bar absolute pressure and at a first temperature level and no steam at a higher temperature level than the first temperature level is generated, wherein the superheated high pressure steam at the first pressure level is at least in part adiabatically and isenthalpically expanded to a second pressure level below the first pressure level such that its temperature level is lowered to a second temperature level, and wherein the first temperature level is selected such that each intermediate temperature level reached at intermediate pressure levels of more than 20 bar during the adiabatic and isenthalpic expansion process is between 5 and 120 K above the dew point of steam at the respective intermediate pressure level during the adiabatic and isenthalpic expansion. A corresponding system (100) is also part of the present invention.

Método e sistema para craqueamento a vapor

método e sistema para craqueamento a vapor. um método de craqueamento a vapor usando um arranjo de craqueamento a vapor (1100-1500) incluindo um ou mais fornos de craqueamento de queima (110), um ou mais trens de resfriamento de têmpera (20) e um ou mais compressores (60) e/ou bombas como equipamento rotativo é proposto, em que uma ou mais correntes de gás de processo são ou são passadas pelo menos através de um ou mais fornos de craqueamento (110) e um ou mais trens de resfriamento de têmpera (20), e em que o equipamento rotativo é pelo menos parcialmente acionado por energia elétrica. de acordo com a invenção, um ou mais arranjos de geração de vapor (30) são ou são operados em associação térmica com um ou mais arranjos de craqueamento a vapor (1100-1500), em que o uso de um ou mais arranjos de geração de vapor (30) pelo menos superaquecido vapor de alta pressão a um primeiro nível de pressão de 3.000 a 17.500 kpa (30 e 175 bar) de pressão absoluta e a um primeiro nível de temperatura e nenhum vapor a um nível de temperatura mais alto do que o primeiro nível de temperatura é gerado, em que o vapor de alta pressão superaquecido no primeiro nível de pressão está em pelo menos em parte expandido adiabaticamente e isentalpicamente para um segundo nível de pressão abaixo do primeiro nível de pressão, de modo que seu nível de temperatura seja reduzido para um segundo nível de temperatura e em que o primeiro nível de temperatura seja selecionado de modo que cada nível de temperatura intermediário seja alcançado em níveis de pressão intermediários de mais de 2.000 kpa (20 bar) durante o processo de expansão adiabática e isentálpica está entre 5 e 120 k acima do ponto de orvalho do vapor no respectivo nível de pressão intermediária durante a expansão adiabática e isentálpica. um sistema correspondente (100) também faz parte da presente invenção.

Method and system for steamcracking

A method of steam cracking using a steam cracking arrangement (1100-1500) including one or more fired cracking furnaces (110), one or more quench cooling trains (20) and one or more compressors (60) and/or pumps as rotating equipment is proposed, wherein one or more process gas streams is or are passed at least through the one or more fired cracking furnaces (110) and the one or more quench cooling trains (20), and wherein the rotating equipment is at least partly driven by electric energy. According to the invention, one or more steam generation arrangements (30) is or are operated in thermal association with the one or more steam cracking arrangements (1100-1500), wherein using the one or more steam generation arrangements (30) at least superheated high pressure steam at a first pressure level of 30 and 175 bar absolute pressure and at a first temperature level and no steam at a higher temperature level than the first temperature level is generated, wherein the superheated high pressure steam at the first pressure level is at least in part adiabatically and isenthalpically expanded to a second pressure level below the first pressure level such that its temperature level is lowered to a second temperature level, and wherein the first temperature level is selected such that each intermediate temperature level reached at intermediate pressure levels of more than 20 bar during the adiabatic and isenthalpic expansion process is between 5 and 120 K above the dew point of steam at the respective intermediate pressure level during the adiabatic and isenthalpic expansion. A corresponding system (100) is also part of the present invention.

Pressure washer apparatus

A pressure washer includes a main line through which, via a high-pressure pump, liquid can be conveyed to a spray opening, and a main valve. The main valve, when in a closed state, prevents liquid from flowing through the main line and, when in an open state, allows liquid to flow through the main line. The main valve is switchable between open and closed via an operator-controlled element. The main line has a suction chamber between the connection and the pump and a pressure chamber between the pump and the spray opening. The pressure chamber is fluidically connected to the suction chamber via a bypass line. A free cross-sectional area of the bypass line is settable via a bypass valve in the bypass line for regulating pressure in the pressure chamber. The bypass valve is adjustable via the operator-controlled element for setting the free cross-sectional area of the bypass line.

Method and system for steamcracking

A method of steam cracking using a steam cracking using a steam cracking system (100) including a first steam cracking furnace unit (1000) or a plurality of first steam cracking furnace units (1000) and a second steam cracking furnace unit (2000) or a plurality of second steam cracking furnace units (2000) is proposed, wherein the first steam cracking furnace unit (1000) or each of the plurality of first steam cracking furnace units (1000) comprises one or more fired steam cracking furnaces (110), the second steam cracking furnace unit (2000) or each of the plurality of second steam cracking furnace units (2000) comprises one or more electric steam cracking furnaces (210), and the first steam cracking furnace unit (1000) or each of the plurality of first steam cracking furnace units (1000) comprises means for preheating at least a part of combustion air provided to its fired steam cracking furnace or furnaces (110) to a temperature level of at least 100 °C. A corresponding system (100) is also part of the present invention.

Method and system for steamcracking

A method of steam cracking using a steam cracking using a steam cracking system (100) including a first steam cracking furnace unit (1000) or a plurality of first steam cracking furnace units (1000) and a second steam cracking furnace unit (2000) or a plurality of second steam cracking furnace units (2000) is proposed, wherein the first steam cracking furnace unit (1000) or each of the plurality of first steam cracking furnace units (1000) comprises one or more fired steam cracking furnaces (110), the second steam cracking furnace unit (2000) or each of the plurality of second steam cracking furnace units (2000) comprises one or more electric steam cracking furnaces (210), and the first steam cracking furnace unit (1000) or each of the plurality of first steam cracking furnace units (1000) comprises means for preheating at least a part of combustion air provided to its fired steam cracking furnace or furnaces (110) to a temperature level of at least 100 °C. A corresponding system (100) is also part of the present invention.

Halteelement und baustoffgreiferanordnung mit einem solchen

Aufzugsanlage

Verfahren und anlage zum steamcracken

Process for producing nanoflakes from g-c3n4/metal composite material

The present invention relates to a process for producing g-C

Pressure washer

A pressure washer has a connection for a source of liquid; a high pressure pump; a main line by way of which liquid via the high pressure pump is conveyable from the connection to a spray opening of the main line; and a supplemental pump for adding an additive to the liquid. The pressure washer is conceived in such a way that the additive by way of the supplemental pump is able to be fed to the main line upstream of the high pressure pump.

High-pressure cleaning appliance

A high-pressure cleaning appliance includes a connection for a liquid source, a delivery pump, a motor for driving the delivery pump, a delivery line through which liquid can be delivered from the connection to a spraying-out opening of the delivery line via the delivery pump, and a valve which is arranged in the delivery line. The motor has two operating states. The two operating states include an off state and an on state. The valve has two valve states, wherein the two valve states include a closed state and an open state. In the closed state, the valve prevents a flow of liquid through the delivery line. In the open state, the valve allows a flow of liquid through the delivery line. The high-pressure cleaning appliance is structurally configured in such a way that the adjustment of the operating state of the motor is possible only if the valve is in the open state.

Hochdruckreinigungsgerät

Die Erfindung betrifft ein Hochdruckreinigungsgerät (1) umfassend einen Anschluss (2) für eine Flüssigkeitsquelle (17), eine Hochdruckpumpe (3), eine Hauptleitung (5), durch die mittels der Hochdruckpumpe (3) Flüssigkeit von dem Anschluss (2) zu einer Ausspritzöffnung (6) der Hauptleitung (5) förderbar ist und eine Zusatzpumpe (4) zur Beimischung eines Zusatzmittels (14) zur Flüssigkeit. Das Hochdruckreinigungsgerät (1) ist so ausgelegt, dass das Zusatzmittel (14) der Hauptleitung (5) stromaufwärts der Hochdruckpumpe (3) durch die Zusatzpumpe (4) zuführbar ist.

Process for producing nanoflakes from g-c3n4/metal composite material

The present invention relates to a process for producing g-C3N4/metal composite material nanoflakes comprising the steps of: (a) providing a starting material comprising or consisting of FePO4, urea and polyacrylonitrile, wherein the starting material is in the form of powder having particles having an average particle size of less than 100 nm, (b) dispersing the starting material in a solvent, wherein the solvent is water, (c) removing the solvent to form a premixture containing the starting material, (d) heating the premixture and pyrolyzing the premixture at a pyrolysis temperature between 200°C and 700°C, preferably between 400°C and 600°C, to form a bulk-g-C3N4/metal composite material, (e) treating the bulk g-C3N4/metal composite material with ultrasound to form g-C3N/4/metal composite material nanoflakes.

Method and system for steamcracking

A method of steam cracking using a steam cracking arrangement (2100-2800) including an electric cracking furnace (10) without a convection zone (12) and further including a quench cooling train (20) is proposed, wherein a process gas stream is passed at least through the electric cracking furnace (10) and the quench cooling train (20). It is provided that that the quench cooling train (20) is operated to comprise at least two distinct cooling steps arranged in either order, wherein in a first one of the cooling steps at least a part of the process gas stream withdrawn from the electric cracking furnace (10) is cooled against vaporizing boiler feed water at an absolute pressure level between 30 and 175 bar and wherein in a second one of the cooling steps at least a part of the process gas stream withdrawn from the electric cracking furnace (10) is cooled against a superheated mixture of feed hydrocarbons and process steam used in forming the process gas stream which is thereby heated to a temperature level between 350 and 750°C. A corresponding arrangement (2100-2800) is also part of the present invention.

Método e sistema para craqueamento a vapor

método e sistema para craqueamento a vapor. é proposto um método de craqueamento a vapor usando um arranjo de craqueamento a vapor (2100-2800) incluindo um forno de craqueamento elétrico (10) sem uma zona de convecção (12) e incluindo ainda um trem de resfriamento por têmpera (20), em que uma corrente de gás de processo é passada pelo menos através do forno elétrico de craqueamento (10) e do trem de resfriamento por têmpera (20). é fornecido que o trem de têmpera (20) seja operado para compreender pelo menos duas etapas de resfriamento distintas dispostas em qualquer ordem, em que em uma primeira das etapas de resfriamento, pelo menos uma parte da corrente de gás de processo retirada do forno de craqueamento elétrico (10) é resfriado contra a vaporização da água de alimentação da caldeira a um nível de pressão absoluta entre 3.000 e 17.500 kpa (30 e 175 bar) e em que, em uma segunda das etapas de resfriamento, pelo menos uma parte da corrente de gás de processo retirada do forno elétrico de craqueamento (10) é resfriado contra uma mistura superaquecida de hidrocarbonetos de alimentação e vapor de processo usado na formação da corrente de gás de processo que é assim aquecida a um nível de temperatura entre 350 e 750 °c. um arranjo correspondente (2100-2800) também faz parte da presente invenção.

Method and system for steamcracking

A method of steam cracking using a steam cracking arrangement (2100-2800) including an electric cracking furnace (10) without a convection zone (12) and further including a quench cooling train (20) is proposed, wherein a process gas stream is passed at least through the electric cracking furnace (10) and the quench cooling train (20). It is provided that that the quench cooling train (20) is operated to comprise at least two distinct cooling steps arranged in either order, wherein in a first one of the cooling steps at least a part of the process gas stream withdrawn from the electric cracking furnace (10) is cooled against vaporizing boiler feed water at an absolute pressure level between 30 and 175 bar and wherein in a second one of the cooling steps at least a part of the process gas stream withdrawn from the electric cracking furnace (10) is cooled against a superheated mixture of feed hydrocarbons and process steam used in forming the process gas stream which is thereby heated to a temperature level between 350 and 750°C. A corresponding arrangement (2100-2800) is also part of the present invention.

Dispositivo para la sujeción de raíles de guía para elevadores de personas y cargas

Dispositivo (1) para la sujeción de raíles de guía (2) para elevadores de personas y cargas que, para la unión de los raíles de guía (2) a una pared de hueco (4) del lado del edificio, presenta una consola de fijación (7) que se puede fijar a los raíles de guía (2) y un contra-perfil (9) que se puede unir a la anterior y a la pared de hueco (4), entre la consola de fijación (7) y el contra-perfil (9) hay dispuesto un aislador (8) y en la consola de fijación (7), el contra-perfil (9), el raíl de guía (2) y/o la pared de hueco (4) están previstos topes como contrasoportes para el aislador (8) para la limitación de un movimiento de expansión, y entre un contrasoporte y el aislador (8) hay conformada una ranura (11, 12), que se caracteriza por que el asilador (8) está fabricado de un elastómero o de goma como material, el tamaño de la ranura (11, 12) está medida de tal modo que la suma de las ranuras (11, 12) más la flexión real del raíl de guía (2) es menor que las flexiones máximas permitidas de los raíles de guía (2) según las normas de seguridad válidas, y los movimientos de expansión del aislador son limitados después de pasar por las ranuras previstas (11, 12).

Urządzenie do zamocowania szyn prowadzących dla dźwigów osobowych i towarowych

Producción de combustibles líquidos (sylvan-liquid fuels) a partir de 2 -metilfurano.

Producción de combustibles líquidos (Sylvan-Liquid-Fuels) a partir de 2-metilfurano. La presente invención describe un procedimiento para la producción de combustible líquido, con un contenido alto en alcanos y bajo en compuestos oxigenados que comprende al menos: - un primer paso de alquilación de 2-metilfurano (denominado comúnmente Sylvan) con un alcohol furánico 2 con la fórmula: 15 donde R^{1} es H o un resto alifático o aromático o hetero-aromático, R^{2} es H o un resto alifático o aromático o hetero-aromático y R^{3} es H, hidroximetil o un resto alifático o aromático o hetero-aromático en presencia de un catalizador - un segundo paso de hidrogenación y deshidratación del compuesto obtenido en el paso 1 en presencia de hidrógeno, utilizando catalizadores de hidrogenación y de deshidratación adecuados.

Production of liquid fuels (sylvan liquid fuels) from 2-methylfuran

Vorrichtung zur Halterung von Führungsschienen für Personen- und Lastenaufzüge

Die Erfindung bezieht sich auf eine Vorrichtung 1 zur Halterung von Führungsschienen 2 für Personen- und Lastenaufzüge, die zur Verbindung der Führungsschiene 2 mit einer gebäudeseitigen Schachtwandung 4 ein beispielsweise zweigeteiltes, an der Führungsschiene 2 festlegbares Winkelprofil 7 und ein mit diesem und der Schachtwandung 4 verbindbares Gegenprofil 9 aufweist, wobei zwischen dem Winkelprofil 7 und dem Gegenprofil ein Isolator aus einem Elastomer angeordnet ist. Um eine Vorrichtung geschaffen zu haben, die körperschallisoliert ausgebildet ist, jedoch einen weitergehenden Wartungsaufwand hinsichtlich der Kontrolle des Anzugsmomentes einer Befestigungsschraube nicht benötigt, ist vorgesehen, dass an dem Winkelprofil 7, dem Gegenprofil und/oder der Schachtwandung 4 Anschläge 9.1 als Widerlager für den Isolator 8 zur Begrenzung einer Ausdehnungsbewegung auf die Schachtwand 4 zu und von dieser weg vorgesehen sind, wobei zwischen einem Widerlager 9 und dem Isolator 8 zumindest bei Erstmontage des Isolators 8 ein Spalt 12 ausgebildet ist.

Anordning til fastgørelse af styreskinner til person- og godselevatorer

Verfahren und anlage zum steamcracken

Producción de combustibles líquidos (sylvan-liquid-fuels) a partir de 2-metilfurano

La presente invención describe un procedimiento para la producción de combustible líquido, con un contenido alto en alcanos y bajo en compuestos oxigenados que comprende al menos: - un primer paso de alquilación de 2-metilfurano (denominado comúnmente Sylvan) con un alcohol furánico 2 con la formula: (2) donde R1 es H o un resto alifático o aromático o hetero-aromático, R2 es H o un resto alifático o aromático o hetero-aromático y R3 es H, hidroximetil o un resto alifático o aromático o hetero-aromático en presencia de un catalizador - un segundo paso de hidrogenación y deshidratación del compuesto obtenido en el paso 1 en presencia de hidrogeno, utilizando catalizadores de hidrogenación y de deshidratación adecuados.

Method of Obtaining Polyoxygenated Organic Compounds

The invention relates to a method of obtaining polyoxygenated organic compounds. The inventive method is characterized in that it comprises the oxidation reaction of a diether, preferably an acetal, with an oxygen source, in the presence of: one or more radical initiating agents, one or more additives that generate a basic reaction medium, and one or more catalysts.

Method and system for steamcracking

Procedimiento para la obtencion compuestos organicos poli-oxigenados.

Procedimiento para la obtención de compuestos orgánicos poli-oxigenados. La presente invención se refiere a un procedimiento para la obtención de compuestos orgánicos poli-oxigenados, caracterizado porque comprende realizar una reacción de oxidación de un diéter, preferente un acetal, con una fuente de oxígeno, en presencia de: - uno o más agentes iniciadores de radicales, - uno o más aditivos que generen un medio de reacción básico, y - de uno o más catalizadores.

Procedimiento para la obtención compuestos orgánicos poli-oxigenados

La presente invención se refiere a un procedimiento para la obtención de compuestos orgánicos poli-oxigenados, caracterizado porque comprende realizar una reacción de oxidación de un diéter, preferente un acetal, con una fuente de oxigeno, en presencia de: uno o más agentes iniciadores de radicales, uno o más aditivos que generen un medio de reacción básico, y de uno o más catalizadores.

Method and system for steamcracking

Method and system for steamcracking

Verfahren und vorrichtung zum umlegen von gütern mittels teilelastischen haltelementen

Die Erfindung betrifft ein Verfahren zum Betrieb einer Greifvorrichtung, aufweisend eine Greifanordnung mit Haltelementen, welche eine teilweise elastisch verformbare Struktur aufweisen, zum Halten eines umzuschlagenden Gutes, umfassend eine Messung eines Spannungszustandes wenigstens eines der Haltelemente mittels Spannungsmessvorrichtungen; und Ermittlung eines momentanen Betriebszustandes der Greifvorrichtung auf Basis des Spannungszustandes des Haltelements; und Steuerung der Greifvorrichtung auf Basis des ermittelten Betriebszustandes.

Method and system for steamcracking