Process and plant for producing ethanol e-fuels from heterogeneous mixes of bioplastic and halogen wastes

Abstract

The present invention relates to a plant and a process for producing ethanol from heterogeneous mixes of bioplastic and halogen wastes.

Description

[0001] Process and plant for the production of alcoholic e-fuels from heterogeneous bio-

[0002] Plastic-halogen waste mixtures

[0003] The present invention relates to a plant and process for producing alcohol from heterogeneous bioplastic-halogen waste mixtures. At a time when waste management and sustainable energy production are of central importance, this invention offers an innovative solution for converting waste into valuable resources.

[0004] Household waste typically consists of a mixture of biogenic waste and packaging materials. The diversity and heterogeneity of plastics in household waste, in particular, complicates recycling. Efficient separation of these plastics is often complex and not always completely possible, which is why much of this waste is thermally recycled in waste incineration plants.

[0005] There are already established processes for the production of alcohol synthesis gases, as an intermediate step in the production of alcohols, particularly from biomass or plastics. For example, publication DE 10 2006 012 313 A1 describes a process for the reduction of carbon dioxide and water using an oxygen ion conductor. DE 102012 010 542 A1 presents a system for the production of synthesis gas. However, the solutions described therein both have their own limitations and disadvantages.

[0006] In addition to these approaches, there are processes such as pyrolysis.

[0007] The object therefore remains to provide an improved plant or process for producing alcohol synthesis gases, in particular from biomass or plastics, or an efficient, reliable, and cost-effective solution for producing alcoholic e-fuels. This object is achieved by the plant according to claim 1 and the process according to claim 7.

[0008] The present invention is based, among other things, on the application of the bubble column principle. This principle utilizes the behavior of bubbles rising in a liquid, which are then purified, separating pyrolysis intermediates from the gas and reintroducing them into the plasmalysis process. This increases the efficiency and purity of the alcohol synthesis gas produced and increases the conversion of waste to the intended product, alcohol.

[0009] The present invention combines several technologies known from the prior art. It integrates the principles of plasmalysis, bubble columns, alcohol synthesis from syngas, electrolysis, and pyrolysis in a novel way. The result is a compact and safe plant and associated process specifically designed to efficiently decompose complex, heterogeneous mixtures of domestic waste, particularly bio-plastic-halogen waste mixtures, into an e-fuel, harmless ash or slag, and clean water.

[0010] A core idea of ​​the invention lies in its duality: It serves both as an energy storage system and a recycling facility. While waste energy is used as one of the main resources, electrical energy is also incorporated into the process to generate the fuel. This represents not only an innovative method for waste recycling but also an efficient way to store and utilize renewable energy.

[0011] Another key step in this process is the comminution of the waste mixture into a granular form to ensure optimal mixing and effective reactions in subsequent processing steps. This crushed granulate is then mixed with a water stream to form a suspension, which is introduced into the plasma bubble column reactor.

[0012] Within the reactor, the suspension is precisely transformed by plasma energy. The plasma is generated by the addition of an electric current, which dries and vaporizes the waste particles, transforming them into a plasma state. After the energy transfer, the plasma bubbles condense, and the previously dissociated atoms recombine into smaller, more volatile molecules such as CO, CO2, H2, H2O, and CH4, which form the alcohol synthesis gas.

[0013] Another important aspect of the invention is the precise adjustment of the C:H and C:H:O ratios, which affect the composition of the synthesis gas leaving the plasma bubble column reactor and the subsequent hydrogen halide neutralizer. This is achieved by the targeted addition of water and the control of the oxygen content using an oxygen separator. The C:H:O ratio results from the chemical formula of the alcohol to be produced and refers to the sum of all C, all H, and all O atoms in the formula. For example, the C:H:O ratio for methanol (CH3OH or CH4O) is 1:4:1 and for ethanol (C2H5OH or C2H6O) it is 2:6:1. It should be noted that the C:H:O ratio of the bio-plastic-halogen waste mixture is subject to natural fluctuations. A tolerance of approximately 5 percent each based on the number of H atoms and O atoms is to be considered in accordance with the invention.It should also be emphasized that water or water vapor is not taken into account when determining the C:H:O ratio, since water and water vapor primarily act as transport media and are therefore not included in the calculation of the ratio.

[0014] The resulting alcohol synthesis gas, often simply referred to as synthesis gas, can contain components such as hydrogen (H2), carbon monoxide (CO), oxygen (O2), carbon dioxide (CO2), water (H2O), and methane (CH4), as well as impurities such as hydrogen halides. It is used primarily to produce an alcohol, preferably methanol. After plasma treatment, the alcohol synthesis gas flows into the hydrogen halide neutralizer. Hydrogen halides, which are hazardous compounds, are converted into harmless substances such as salt, water, and CO2 in this neutralizer, thus effectively suppressing them.

[0015] The alcohol synthesis gas then flows through a catalyst and is transformed into a mixture of alcohol and water as it passes through the catalyst. The subsequent separation of this mixture produces various streams: water, alcohol, incompletely converted alcohol synthesis gas, an oxygen-rich stream, and an outlet for non-reacting gases such as nitrogen. This oxygen-rich stream, which can consist of water, CO2, or a combination of both, is fed to the oxygen separator to precisely regulate the oxygen content in the system. A particular focus is on the role of water in the process. Water serves as a transport medium and energy moderator. It transports the granular waste particles as a suspension into and out of the plasma bubble column reactor.Evaporating a portion of the used water in the reactor ensures high plant safety, as the high energy of the plasma does not reach the inner surface of the reactor. The subsequent condensation of the water in the catalyst and separation system produces ultrapure water, which is crucial for the oxygen separator. This ultrapure water, which mainly contains traces of alcohol, is either fed into the oxygen separation system or removed from the system. Externally supplied water for suspension formation can also be contaminated wastewater.

[0016] The invention also integrates material recycling systems, such as the recirculation of incompletely converted alcohol synthesis gas and heat exchangers, to maximize process efficiency. This ensures not only the quality of the produced alcohol, but also the safety, stability, efficiency, and environmental friendliness of the entire process.

[0017] In summary, the device according to the invention offers a sustainable and efficient method for converting bio-plastic-halogen waste mixtures into e-fuel, thereby representing a significant advance in the field of waste recycling and sustainable energy production.

[0018] In the context of the present invention, the term 'bio-plastic-halogen waste mixture' refers to a mixture containing both biological waste and plastic waste and halogen-containing compounds. While the biological waste originates from natural, organic sources, the plastic waste represents man-made polymers. The halogen-containing compounds are often contaminants that enter the mixture through certain plastics, such as PVC, or through additives such as fluorine-containing plasticizers.

[0019] In the context of the present invention, the term 'synthesis gas' refers to a versatile gas mixture that may primarily consist of hydrogen (H2), carbon monoxide (CO), water (H2O), carbon dioxide (CO2) and methane (CH4).

[0020] Alcohol synthesis gas is a specific variant of synthesis gas optimized for the production of alcohols, especially methanol and ethanol. It is characterized by a characteristic C:H:O ratio, which is derived from the chemical formula of the desired alcohol. For example, the C:H:O ratio of methanol (CH3OH) is 1:4:1. In addition to the main components, alcohol synthesis gas may also contain small amounts of other gases.

[0021] Hydrogen halides are a group of chemical compounds consisting of hydrogen (H) and a halogen atom (fluorine, chlorine, bromine, iodine, or astatine). The best-known representatives of this group are hydrogen fluoride (HF), hydrogen chloride (HCl), hydrogen bromide (HBr), and hydrogen iodide (HI). These compounds can form when halogens contained in waste, such as chlorine from PVC or fluorine from certain plasticizers, react with hydrogen under certain conditions.

[0022] Hydrogen halides are problematic for several reasons:

[0023] 1. Corrosivity: Hydrogen halides, especially HF and HCl, are highly corrosive and can attack metals and other materials used in plant and equipment. This can lead to premature wear and potential leaks.

[0024] 2. Toxicity: Some hydrogen halides, especially HF, are highly toxic and can cause serious injury if they come into contact with the skin, eyes, or if inhaled.

[0025] 3. Environmental impacts: When released into the environment, hydrogen halides can contribute to acid rain and contaminate water sources. This can have negative effects on plants, animals, and humans.

[0026] 4. Process disruption: In industrial processes, hydrogen halides can cause undesirable side reactions and impair the quality of the final product.

[0027] Because of these hazards, it is important to minimize or effectively control and neutralize the formation of hydrogen halides in processes that treat waste.

[0028] In the context of the present invention, the term 'hydrogen halide neutralizer' refers to a system designed to prevent or reduce the formation of hydrogen halides. These hydrogen halides can be formed when halogens present in waste, such as chlorine or fluorine, react under certain conditions.

[0029] Hydrogen halide neutralizer: The hydrogen halide neutralizer primarily serves to neutralize the hydrogen halides formed in alcohol synthesis gas. Its main functions are:

[0030] 1. Neutralization: The inhibitor neutralizes hydrogen halides by converting them into less harmful compounds such as salts, CO2 or water.

[0031] 2. Protection of plants and equipment: It protects metals and other materials from the corrosive effects of hydrogen halides.

[0032] 3. Safety and environmental protection: It prevents the formation or release of toxic hydrogen halides, thus contributing to the protection of workers and the environment.

[0033] In the application described here, the hydrogen halide neutralizer consists of materials such as calcium carbonate or sodium carbonate, which are particularly effective in neutralizing hydrogen halides due to their chemical properties.

[0034] A plasma bubble column reactor extends the concept of the state-of-the-art bubble column through the use of plasma. Here, the supplied gas is converted into plasma by a plasma generator and rises through the suspension as plasma bubbles. This enables chemical reactions known as pyrolysis or plasmalysis at temperatures and conditions unattainable in conventional bubble columns. The suspension surrounding the plasma bubbles allows the high energy density of the plasma to be restricted to a localized area, thus safely containing it spatially and feeding it into the waste granules contained in the suspension.

[0035] Main features of the plasma bubble column reactor are:

[0036] 1. Plasma bubbles: The gas is converted into plasma and rises as plasma bubbles.

[0037] 2. Chemical reactions: Pyrolysis or plasmalysis reactions occur within the plasma bubbles and in the suspension.

[0038] 3. Transformation of plasma bubbles: The plasma bubbles transform into normal gas bubbles and mix with other gases.

[0039] 4. Reactor: The main purpose is to carry out chemical reactions.

[0040] 5. Plasma generator: It enables the formation and control of the plasma.

[0041] 6. Electricity supply system: It supplies the plasma generator with the required energy.

[0042] In summary, the plasma bubble column reactor combines the advantages of the bubble column with plasma technology for efficient chemical processes.

[0043] In chemistry and chemical engineering, a suspension is a heterogeneous mixture of solid particles dispersed in a liquid without dissolving in it. The solid particles are suspended in the liquid, meaning they float in the liquid without settling as long as the suspension is kept in motion.

[0044] In the plasma bubble column reactor, a suspension of shredded bio-plastic-halogen waste mixtures and water is used, through which plasma bubbles rise and in which chemical reactions take place. The suspension is created by a shredder that breaks down solid materials into smaller particles. In the context of the plasma bubble column reactor, it serves to prepare bio-plastic-halogen waste mixtures for the suspension.

[0045] A plasma generator is a specialized device used to convert a gas into a plasma state. Plasma, often referred to as the fourth state of matter, consists of ionized gas particles containing both positive ions and free electrons. This ionized state enables a variety of chemical reactions that would not be possible in a normal gas state.

[0046] In the context of the plasma bubble column reactor, the plasma generator has the following key functions and features:

[0047] 1. Gas ionization: The plasma generator takes the gas supplied from below and ionizes it, creating plasma bubbles. These plasma bubbles then rise through the liquid in the bubble column. 2. Energy supply: To convert the gas into a plasma state, the plasma generator requires a continuous supply of electrical energy. A special electrical supply system ensures that the plasma generator always has the required energy available.

[0048] 3. Control and regulation: The plasma generator can be controlled to produce plasma with specific properties and in specific quantities. This allows precise control over the chemical reactions taking place in the plasma bubble column reactor.

[0049] 4. Integration into the reactor: The plasma generator is directly integrated into the plasma bubble column reactor, enabling efficient conversion of the supplied gas into plasma and direct interaction with the surrounding suspension.

[0050] 5. Promotion of pyrolysis and plasmalysis reactions: The generation of plasma in the reactor creates the conditions for pyrolysis and plasmalysis reactions. These reactions are often not only faster and more efficient than conventional chemical processes, but are also characterized by the ability to break any molecular bonds, as the plasma provides a high amount of energy.

[0051] In summary, the plasma generator is an essential element of the plasma bubble column reactor, which enables the conversion of gas into plasma and subsequently dissolves the molecular cohesion of the waste particles supplied via suspension, thus creating the basis for the specialized chemical reactions within the reactor.

[0052] A separation system is a device or process used to separate different components of a mixture. In chemical engineering and biotechnology, separation systems are essential for obtaining pure products from reaction mixtures or removing unwanted byproducts.

[0053] In the specific context of the described plant, the separation system has the following key functions and features:

[0054] 1. Separation process: The separation system uses specialized separation processes such as distillation or reverse osmosis. While distillation relies on the different boiling points of the components to separate them, reverse osmosis uses a selective membrane process to separate molecules or ions of different sizes.

[0055] 2. Product recovery: The main goal of the separation system is to separate alcohol and water from the reaction mixture. This allows for the recovery of pure alcohol and water as separate products.

[0056] 3. Formation of material streams: Separation of the mixture produces various material streams. These include water, alcohol, and incompletely converted alcohol synthesis gas.

[0057] 4. Oxygen-rich stream: Another important product of the separation system is an oxygen-rich stream. This can consist of water, CO2, or a combination of both. This stream is particularly important because it is fed to the oxygen separator. This allows for precise control of the oxygen content in the system, which is crucial for downstream processes.

[0058] 5. Separation of inert gases: The separation system also has an outlet for gases that do not participate in the reaction to produce alcohol. These include traces of inert gases and nitrogen. These gases are removed from the system to ensure the quality and efficiency of the process.

[0059] In summary, the separation system is an essential component of the plant, which not only enables the extraction of pure alcohol and water, but also contributes to the regulation of the oxygen content in the system and the separation of unwanted gases.

[0060] In this process, an oxygen separator is used to remove oxygen from the oxygen-rich fluid (gas mixture or liquid) extracted from the separation system. In the present invention, this separator can be implemented in the form of an electrolyzer or a CO electrolyzer.

[0061] 1. Electrolyzer:

[0062] • An electrolyzer uses electrolysis to split water (FW) into its components, hydrogen (H2) and oxygen (O2). This is done by applying an electrical voltage to electrodes immersed in an electrolyte solution.

[0063] • Oxygen is released at the anode (positively charged electrode), while hydrogen is released at the cathode (negatively charged electrode).

[0064] 2. CO electrolyzer:

[0065] • A CO electrolyzer, also known as a carbon dioxide electrolyzer, specializes in converting carbon dioxide (CO2) into carbon monoxide (CO) and oxygen (O2) using electrical current.

[0066] • Similar to a conventional electrolyzer, an electrical voltage is applied to electrodes immersed in a suitable electrolyte solution.

[0067] • Oxygen is released at the anode, while carbon monoxide is produced at the cathode.

[0068] In both cases, whether electrolyzer or CO electrolyzer, the use of electrical current promotes a chemical reaction that leads to the release and thus the separation of oxygen.

[0069] The catalyst plays a central role in the invention by efficiently converting alcohol synthesis gas into alcohol and water. It accelerates the reaction, ensures product quality, and works in coordination with other process components. After its function, the product mixture is further separated.

[0070] The gas introduction system directs the gas to the plasma generator, primarily using low-oxygen gas and offering the option of incorporating recycle gases such as unreacted alcohol synthesis gas. It ensures optimal conditions for plasma formation while providing safety and adaptability to various waste materials.

[0071] The recirculation system in the described invention is a simple but essential mechanism responsible for the efficient recirculation of an oxygen-rich stream from the separation system to the oxygen separator. The system directs the oxygen-rich stream removed from the separation system, which may contain water, CO2, or a mixture of both, into the oxygen separator.

[0072] The water recycling system plays a central role in the efficient use and reuse of water within the described invention. After the water has been separated from the ash or slag in the ash / slag separation unit, it is returned to the suspension system via the water recycling system. Here, the recycled water is combined with the granular bioplastic-halogen waste mixture and with externally supplied water to form a suspension.

[0073] The ash / slag separation unit is responsible for separating water from ash or slag. The unit receives an ash / slag suspension from the plasma bubble column reactor and separates the water from the solid components. This can be done by filtration, centrifugation, sedimentation, or decantation, for example. The resulting water is then returned via the water recycling system, while the separated ash or slag is available for further processing steps or disposal.

[0074] Material recycling is a system or method that aims to return certain materials or substances that were not fully converted or utilized during a process to the original or a subsequent process step. This serves to increase the efficiency of the overall process, conserve resources, and minimize waste or losses.

[0075] In the context of the present invention, material recirculation refers specifically to the unconverted alcohol synthesis gas. This gas is captured in the separation system and, instead of being treated as waste or released, is returned to the process via the material recirculation system. This ensures that the alcohol synthesis gas is utilized to its maximum potential and that the overall process is more efficient and resource-efficient.

[0076] The use of material recycling is a sign of sustainable and environmentally conscious process design, as it helps to reduce the consumption of raw materials and minimize environmental impacts.

[0077] A preferred embodiment of the present invention is described in more detail below with reference to the figure. The figure shows a schematic view of a plant for producing alcohol from heterogeneous bio-plastic-halogen waste mixtures according to a preferred embodiment of the present invention.

[0078] The plant comprises a shredder (10) for bio-plastic-halogen waste mixtures, a suspension system (12) for forming a suspension of shredded bio-plastic-halogen waste granules and water, a plasma bubble column reactor (14), a plasma generator (36) integrated therein, an electricity supply system (16) for supplying energy to the plasma generator (36), an oxygen separator (18) for controlling the C:H:O ratio of the mixture, a hydrogen halide neutralizer (20) for reducing hydrogen halide impurities, a catalyst (22) for converting the alcohol synthesis gas into an alcohol-water mixture, a separation system (24) for separating alcohol, water and alcohol synthesis gas, a recirculation system (25) for recirculating an oxygen-rich fluid, a water recycling system (26) for reusing the water from the process, an ash- / slag separation unit (32) for separating ash or slag,and a gas introduction system (34) for low-oxygen gas from the oxygen separator (18) into the plasma bubble column reactor (14).

[0079] A bio-plastic-halogen waste mixture is fed either manually or automatically to the shredder (10), which can be, for example, a hammer mill, a cutting mill system, or a ball mill. The latter is reduced in size in the shredder to particles ranging in size from 1 mm to 30 mm. The reduced particles are then mixed with water in the suspension system, which can be, for example, a paddle agitator, a drum mixing system, or a screw mixing system, to produce a bio-plastic-halogen waste mixture particle-water suspension. The ratio of solids to water in the suspension is preferably between 1:10 and 1:50.

[0080] The water required for the suspension comes from both external sources (see the arrow on the left) and from the water recycling system (26), which recycles water from the ash / slag separation unit (32). The amount of water supplied depends on the nature of the bio-plastic-halogen waste mixture. The C:H ratio of a dry starting substrate serves as a guideline, with the target ratio in the alcohol synthesis gas (for methanol) being 1:4. Due to varying waste compositions, an average C:H ratio of 1:2 is assumed. The water content of the waste is estimated and is typically considered a 1:1 mixture of dry matter and water. The amount of external water required in operation is determined by backward balancing based on the alcohol produced and the composition of the alcohol synthesis gas.The material flows entering and leaving the separation system (24) are continuously monitored using suitable measuring devices, such as those based on infrared spectroscopy (IR), tunable diode laser absorption spectroscopy (TDLAS), or Fourier transform infrared spectroscopy (FTIR). Depending on the balance, the required water is fed to the suspension system (12). If the waste has a high water content, it may be necessary to remove water from the system. In such a case, no external water is added; instead, water from the separation process is discharged to the environment. The resulting suspension of bio-plastic halogen waste and water is fed to the plasma bubble column reactor (PBSR) (14) for further processing. Furthermore, the oxygen-depleted gas is added to the plasma bubble column reactor (14) via the gas introduction system (34).A three-phase flow is created in the PBSR (14), consisting of the gas phase (plasma and gas), the solid phase (waste particles), and the liquid phase (water in the suspension). Density differences between these phases create circulation flows in the PBSR (14), ensuring continuous mixing of the substrates. Circulation flows also form within the gas bubbles, transporting particles to the bubble surface where they coalesce with the surrounding water phase. Both liquid and solid particles in the gas phase are absorbed by the liquid phase, resulting in a purification effect of the gas in the bubble. A gas mixture (alcohol synthesis gas) consisting solely of the gases volatile at approximately 150–200 °C is present at the PBSR outlet.

[0081] As the name PBSR suggests, the reactor is not exclusively dominated by a solid-liquid-gas regime. A plasma-gas-liquid-solid system is created, particularly in the area of ​​the plasma generator (36). The oxygen-poor gas supplied via the gas introduction system (34) is converted into plasma by electric current using a plasma generator, more specifically, a welding torch using the Arcatom welding process (Langmuir torch).

[0082] The plasma bubbles rise due to density differences in the PBSR, ensuring constant mixing. The high plasma energy is transferred to the environment, causing the bio-plastic halogen waste in the suspension to dry, vaporize, and ultimately dissociate at the atomic level. This creates a three-phase flow of gas, liquid, and solid particles. Backmixing, circulation flows, and resulting centrifugal forces separate the waste into light and heavy, as well as volatile and less volatile compounds. The reaction of the waste particles with the plasma produces gas and ash or slag particles. The high water-to-solid ratio in the suspension ensures that the plasma / gas phase remains smaller in volume than the surrounding water, thus maintaining fluidity while safely containing the plasma zone.Due to the high water content and the operating pressure within the PBSR, the temperature of the PBRS is maintained at around 183 °C (boiling point of water at 10 bar vessel pressure). The heavier ash / slag particles collect at the bottom of the PBSR and can be removed there. This ash / slag-water suspension is fed to the ash / slag separation unit, where it is separated into water and ash or slag. Separation is achieved through a combination of filtration (for particle separation) and reverse osmosis (for salt separation from the water).

[0083] The separated water is returned to the suspension system and undergoes the process again. At the top, the gas phase, i.e. the alcohol synthesis gas, leaves the PBSR. Since the alcohol synthesis gas may be contaminated with hydrogen halides at the PBSR outlet, it is fed to the hydrogen halide neutralizer (20). In this neutralizer, the hydrogen halides react with the neutralizer material, for example, calcium carbonate or sodium carbonate. Due to their chemical properties, these substances react with the hydrogen halides and are converted into harmless salt, water, and CO2. The hydrogen halide neutralizer (20) is therefore a consumable and must be replaced regularly. After treatment in the hydrogen halide neutralizer (20), the resulting alcohol synthesis gas is free of hazardous and highly corrosive components.This purified gas is converted into alcohol and water in the catalyst, which, for example, consists of a bed of iron spheres. Since the conversion of the alcohol synthesis gas into water and alcohol is exothermic, the catalyst must be cooled. Established cooling methods already exist, but in the context of this invention, in-process energy recovery could also be used.

[0084] The mixture extracted from the catalyst consists of water, alcohol, and the incompletely converted reactants, i.e., the residues of the alcohol synthesis gas. To separate the water and alcohol from the synthesis gas residues, the mixture is preferably cooled to 40 °C or below. A separator is suitable for this gas-liquid separation. However, this separation represents only one aspect of the tasks of the separation system (24). The system has additional components specifically designed for the separation of nitrogen and other inert gases. Nitrogen separation can be achieved by pressure swing adsorption (PSA) or suitable membrane separation processes. Distillation processes or combined techniques of adsorption / desorption and distillation are also applicable. It is particularly important to emphasize that the separation system can also be used to produce technically pure alcohol (with a purity of approximately98 vol%) and technically pure water (with a purity of approximately 99.9 mass%). Therefore, a combined distillation plant is the preferred method here. At the separation system, both the incoming and outgoing masses and their composition are precisely measured. Together with the measured mass flow of the bio-plastic-halogen waste mixture, an atomic balance enables the precise determination of the required amount of water, which must either be added externally to the suspension system (12) or removed at the separation system (adjustment of the C:H ratio). This balance also provides information about the amount of oxygen to be removed in the oxygen separator (18) (adjustment of the C:H:O ratio). The balance is performed by a computer and then used to control the plant and product quality.

[0085] The final integral process step is the oxygen separator (18), which can be implemented, for example, in the form of an electrolysis system. Depending on the amount of oxygen to be separated, specified by a computer (or controller), an oxygen-rich stream is fed to the oxygen separator (18) via the recirculation system (25). This stream, referred to as the "oxygen-rich stream," is preferably pure water.

[0086] List of reference symbols:

[0087] 10 - Shredder

[0088] 12 - Suspension system

[0089] 14 - Plasma bubble column reactor

[0090] 16 - Electricity supply system

[0091] 18 - Oxygen separator

[0092] 20 - Hydrogen halide neutralizer

[0093] 22 - Catalyst

[0094] 24 - Separation system

[0095] 25 - Return system

[0096] 26 - Water recycling system

[0097] 30 - Material returns

[0098] 32 - Ash / slag separation unit

[0099] 34 - Gas introduction system

[0100] 36 - Plasma generator

Claims

Patent claims 1. Plant for the production of alcohol from heterogeneous bio-plastic-halogen waste mixtures, comprising: i. a shredder (10) for bio-plastic-halogen waste mixtures, ii. a suspension system (12) for forming a suspension of shredded bio-plastic-halogen waste granules and water, iii. a plasma bubble column reactor (14) with a plasma generator (36), iv. an oxygen separator (18), v. a hydrogen halide neutralizer (20), vi. a catalyst (22) for converting the hydrogen halide neutralizer (20) into a mixture with alcohol and water, and vii. a gas introduction system (34) for introducing gas into the suspension of comminuted bio-plastic halogen waste granulate and water in the plasma bubble column reactor (14).

2. Plant according to claim 1, further comprising: a separation system (24) which divides the mixture of substances removed from the catalyst (22) into separate streams, including but not limited to alcohol, water, inert gases, nitrogen, unreacted alcohol synthesis gas and an oxygen-rich stream consisting of, for example, H2O, CO2 or a combination thereof.

3. Plant according to one of the preceding claims, further comprising: material recirculation means (30) for recirculating unreacted alcohol synthesis gas from the separation system (24) either to a location upstream of the catalyst (22) or via the gas introduction system (34) into the plasma bubble column reactor (14).

4. Plant according to one of the preceding claims, further comprising: an ash / slag separation unit (32) and a water recycling system (26) for returning water from the ash / slag separation unit (32) to the suspension system (12).

5. Plant according to one of the preceding claims, dependent on claim 2, further comprising: a recirculation system (25) for transferring an oxygen-rich material stream from the separation system (24) to the oxygen separator (18).

6. Plant according to one of the preceding claims, further comprising: a supply line which serves to supply external water into the suspension system (12) and / or enables water to be discharged from the separation system (24) to the environment.

7. Process for alcohol production from heterogeneous bio-plastic-halogen waste mixtures, comprising the following steps: i. Processing the bio-plastic-halogen waste mixtures by comminution using a comminutor (10), ii. Combining the comminuted material with water using a suspension system (12) to produce a suspension, iii. Introducing the suspension into a plasma bubble column reactor (14) and generating a plasma in the plasma bubble column reactor (14) to treat the suspension, iv. Neutralizing hydrogen halide impurities in the resulting synthesis gas taken from the plasma bubble column using a hydrogen halide neutralizer (20), v. Catalyzing the synthesis gas to form an alcohol-water mixture using a catalyst (22), vi. Separating nitrogen, alcohol and water from the catalysed synthesis gas in a separation system (24), vii.Separating oxygen from the material stream taken from the separation system (24) in an oxygen separator (18). Introducing oxygen-poor gas from the oxygen separator (18) into the plasma bubble column reactor (14) to form a 3-phase dispersion.

8. The method according to claim 7, wherein in the separation system (24) the mixture of substances removed from the catalyst (22) is separated into separate streams, including but not limited to alcohol, water, inert gases, nitrogen, unreacted alcohol synthesis gas and an oxygen-rich stream consisting of, for example, H2O, CO2 or a combination thereof.

9. The method according to claim 7 or 8, further comprising: recycling unreacted alcohol synthesis gas from the separation system (24) either to a location upstream of the catalyst (22) or via a gas introduction system (34) into the plasma bubble column reactor (14) by means of material recirculations (30).

10. The method according to any one of claims 7-9, wherein a mixture of substances is removed from the plasma bubble column reactor (14) and fed to an ash / slag separation unit (32), wherein preferably water from the ash / slag separation unit (32) is recycled into the suspension system (12) by means of a water recycling system (26).

11. The method of any one of claims 7-10, further comprising returning an oxygen-rich fluid from the separation system (24) to the oxygen separator (18).

12. The method according to any one of claims 7-11, further comprising supplying external water to the suspension system (12) and / or discharging water from the separation system (24) to the environment.

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