TW200817501A - A control system for the conversion of a carbonaceous feedstock into gas - Google Patents

Abstract

The present invention provides a control system for the conversion of carbonaceous feedstock into a gas. In particular, the control system is designed to be configurable for use in controlling one or more processes implemented in, and/or by, a gasification system for the conversion of such feedstock into a gas, which may be used for one or more downstream applications. Gasification processes controllable by different embodiments of the disclosed control system may include in various combinations, a converter, a residue conditioner, a recuperator and/or heat exchanger system, one or more gas conditioners, a gas homogenization system and one or more downstream applications. The control system operatively controls various local, regional and/or global processes related to the overall gasification process, and thereby adjusts various control parameters thereof adapted to affect these processes for a selected result. Various sensing elements and response elements are therefore distributed throughout the controlled system and used to acquire various process, reactant and/or product characteristics, compare these characteristics to suitable ranges of such characteristics conducive to achieving the desired result, and respond by implementing changes to in one o more of the ongoing processes via one or more controllable process devices.

Description

200817501 IX. DESCRIPTION OF THE INVENTION: TECHNICAL FIELD OF THE INVENTION The present invention relates generally to control systems and, more particularly, to control systems for converting a carbonaceous feed to a gas. [Prior Art] r Vaporization UasificatioW is a process in which a carbonaceous feed such as a solid waste (MSW) or coal is converted into a combustible gas. The gas produced can then be used to generate steam or as a feedstock that can produce chemicals or liquids. a ^ ^ ^ α τ : μ t μ^ ^ ^ Vapours for internal treatment and/or external use, or for evaporation to generate electricity; directly in a gas turbine or gas engine for combustion) Feed of chemicals such as fertilizers; extraction of fen ^ ^ ^ ^ 11 and carbon monoxide for industrial fuel gas; and other industrial applications. In general, the vaporization process consists of charging the 々&\匕• liver' carbon feed with controlled and or straightened oxygen (sometimes it can also contain a certain amount of < a few) Feed into a heated chamber (vaporizer). Different from incineration or combustion under the action of excess oxygen under the action of milk to produce co2, η2ο, S0x and Ν0χ, a few systems will produce a kind of C0, Η2, H2S and ν 3 之 全 全 全 全 全 全 全 全 全 全 全 全 租 租 租 租 租 租 租 租 租 租 租 租 租 租 租 租 租 租 租 租 租 租 租 租Useful feeds include solid waste in any city, waste from industrial activities and biomedical waste, sewage, sludge, coal, heavy 200817501 oil, petroleum coke, heavy refining residue Residues, hydrocarbon contaminated soil, biomass, agricultural waste, tires and other toxic waste. Depending on the source of the feed, the volatiles may include h2〇, H2, N2, 〇2, CO, CH4, H2S, NH3, C2H6 and unsaturated hydrocarbons (eg, fast, hydrocarbon, aromatic, tar, Hydrocarbon liquid (oil) and char (char) (black and gray). . . . : As the feed is heated, the first component of the composition to be evaporated is water. The temperature of the dry feed is then increased and thermal cracking begins. During thermal cracking, the feed is thermally decomposed to produce tar, phenol, and lighter volatile hydrocarbon gases, while the feed is also converted to char. The char contains a solid residue composed of organic and inorganic materials. After thermal cracking, the char content of the char can be higher than the original dry feed and can be used as a source of active discs. At high temperatures (>12〇(rc) operated vaporization process or in systems with high temperature zones, inorganic minerals are melted or vitrified to form a molten glassy object called “melting” Slag. Because slag is in a molten or vitrified state, it is known to be non-toxic and can be disposed of directly as a landfill or as a stone, 'base or other building material. Sale. At present, there is a growing tendency to treat waste materials by incineration because they consume a large amount of fuel during heating and produce waste that needs to be further discarded (eg, residual waste [and can be converted into useful gases] Materials with solids There are many ways to achieve a vaporization process, depending on the following four main engineering factors: · The environment inside the vaporizer (oxygen content or air or steam 6 200817501

The design of the vaporizer itself, the internal and external heating components and the operating temperature of the process. Factors affecting the quality of gas products include: composition and particle size of the composition; heating rate of the vaporizer; residence time; work waste design (including the use of: dry or I-type system W; dry ash or slag material removal) In addition to the design of the system; whether direct or indirect heat production and transfer methods are used; and slag removal systems. Vaporization is generally carried out at temperatures between 65 and 120 〇t, even at temperatures up to 100 atm. A variety of systems have been proposed to capture the heat of the vaporization process and further generate electricity using the captured heat: generally referred to as combined cycle systems. , .. '. . . . . . , · . . . . -.: ... The energy of the product gas, the large amount of recoverable heat generated by the process and the output of the vaporization system, can generate substantially enough electricity to drive the process, thereby reducing Partial power consumption. The amount of electricity required to vaporize the carbon-containing feed in tons, depending on the chemical composition of the feed. If the gas produced by the vaporization process contains a wide range of volatile substances, for example, "low The type of gas produced by a carbonaceous feedstock in a low temperature vaporizer, which is generally referred to as r gas (burning). If the characteristics of the feed and the conditions in the vaporizer can produce c〇 and % as the main chemistry The gas of the component, such a gas is called "syngas." Some vaporization equipment uses a technology that converts crude gas or crude syngas into a more refined gas before cooling, and uses gas quality. Adjusting the system for cleaning. Commercially, the technology of vaporizing materials by plasma heating technology has been used for many years. Plasma is a high-temperature luminescent gas (which is at least partially free), and 200817501 is composed of gaseous atoms, gaseous ions and electrons. Any gas can be used in this manner to form a plasma. This allows control of the chemical reaction within the electrical device, as the gas can be neutral (eg, argon, helium, atmosphere), reducing (eg, hydrogen, decane, Ammonia, carbon monoxide) or oxidizing (eg 'oxygen, oxidizing'). In this phase: the plasma is electrically neutral. * * ·. .,.. - used in some vaporization systems Rong heating drives the vaporization process at the south temperature. . . . and / or when the gaseous molecules contact the electric heat and dissociate into their individual constituent atoms::·····., with or without other wheels In the case of an inverting reactant, refine the outgassing/synthesis gas by converting, recombining or reforming long-chain volatiles and tars into small molecules. Many of these atoms will react with other wheeled molecules to form The new molecules, as for others, will be combined again into their original molecules. As the temperature of the molecules in thermal contact with the plasma drops, all atoms will be re-eluted. Since the stoichiometry of the input gas can be controlled, the output The stoichiometry of the gas can also be controlled, for example, to produce a large amount of oxidized and a small amount of oxidizing. - · ... * , the extremely high temperature (3000~7000t:) that can be achieved by plasma heating makes the high temperature

Become a useful product. A desired compound and requires further processing to convert the carbonaceous feed to a gaseous state. 8 200817501 Remove unwanted metals, sulfides, and ash from the gas. For example, dry filtration is generally used. Or a wet scrubbing system to remove particulate matter and ritual gases from the gases generated during vaporization. A variety of vaporization systems have been developed that contain gases that can be processed to vaporize the gas. The above has briefly introduced the factors that need to be considered when designing various systems. These factors are disclosed in U.S. Patent Nos. 6,686,556 and 6,630. No. 113, No. 6, 3, 80, 507, No. 6, 215, 678, No. 5, 666, 89, No. 5, 798, 497, 5, 756, 957, and the US Patent Application Publication No. 2004/0251214 No. 2002/0144981. There are also many related technologies for vaporizing coal to produce multi-purpose syngas. . . . . . . . . . . . . . . In the following patent cases: US patent Nos. 4,141,694, 笫4,181,5 04, 4,208,191, 4,410,336, 4,472,1 72, 4,606,799, 5,331,906, 5,486,269 and 6,200,430 . Previous technologies and systems did not adequately address the issues that must continue to change and must be faced. Some of these vaporization systems disclose an adjustment member that adjusts the process of producing a useful gas from a vaporization reaction. Therefore, if the former technology can provide energy, the effective vaporization (that is, the process of optimizing the overall efficiency of the process and / or the process of including the overall process) carbon-containing feed < system, will be extremely advantageous. Accordingly, there is a need for a control system that can convert a carbonaceous feed to a gas that overcomes the shortcomings of known control systems. This background description is only a description of the known knowledge of the applicant, and it is not intended to be construed as a limitation of the invention. 9 200817501 SUMMARY OF THE INVENTION *. . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . According to one embodiment, a control system for controlling a vaporization process is provided to convert a carbonaceous feed to a gas suitable for immediate use in a selected downstream application. The system includes: one or more sensors 'for one of the properties of the gas; one or more computing platforms, the communication link to the one or more sensors to access the characteristic I representative of the inductive characteristic; The characteristic value is compared with a preset range of one of the class values (which defines the characteristics of the gas suitable for the selected downstream application); and one or more process control parameters are honored, which contributes to Holding the characteristic value in the preset range; and a plurality of response elements operatively linked to the one or more processing devices and operable to make the processing effective to adjust the characteristics of the gas' Bonding to the one or more calculated process control parameters and operating the devices according to the parameters v * . . . , [Embodiment] . * ♦ . . . * Unless otherwise defined, the techniques and sciences used herein The term "about" is used herein to encompass the numerical value + Λ 10%, as used herein by those skilled in the art to which the present invention pertains. It is to be understood that any value recited herein, whether or not explicitly stated to be in the approximate range, is intended to cover the stated value herein, the terms "carbonaceous feedstock" and "feedstock" are included. Any of the 10 200817501 carbon materials used in the vaporization process of the present invention, including but not limited to: any waste material, 咕山琛 charcoal (including low-grade, high-sulfur coal that is not suitable for use in coal thermal power plants) ), petroleum coke, heavy oil, biomass, sludge, from Taiji: (2) Sludge and agricultural waste from non-product mills or paper baskets... Waste materials suitable for vaporization include valuable and harmless waste Things, such as municipal waste, waste from industrial activities (paint effluent, paints that do not conform to regulations, used sorbents), automotive fluffs, used tires, and biomedical waste • Any carbonaceous material that is not suitable for recycling, including non-recyclable plastics: sewer sludge, coal, heavy oil, petroleum coke, children's refining residue, refining waste 'carbon hydride Contaminated soil waste and biomass, agricultural waste, wheeled, toxic waste, industrial waste and biomass β Examples of biomass that can be used in the vaporization process include (but are not limited to) · Abandoned or fresh wood, fruits and vegetables And residue after grain processing, pulp mill residue, straw, grass, and excrement.

The term "sensing element" is defined as any element of the system that is used by Han juice to sense the characteristics of a process, a process, a process input, or a process output. To represent, adjust, and/or control the characteristic values of one or more shoulders, regions, and/or overall processes of the system. Inductive elements in a vaporization system are considered to include, but are not limited to, sensors, detectors, monitors, analyzers, or any combination thereof, which can be used to sense processes, fluids and compositions, and/or the like. Characteristics, material location and/or placement, and operating conditions. The temperature of the sensing device, the pressure, the flow rate, and any processing device used at any given location in the system can be understood by any of the skilled persons in the field. Although it is semantically related to the vaporization system, it is not necessarily absolutely relevant to the present invention, and thus the sensing elements indicated herein are not exhaustive or limited to the scope of the embodiments. .* ... * -* · The term "response element" is defined as any element of the system designed to respond to an inductive characteristic, based on one or more preset, calculated, fixed sums / or an adjustable control to operate the processing element connected thereto (operably), wherein the - or multiple control parameters . . . '* . · ' · . . are defined as providing the desired processing Green fruit. Vaporization system Yuan Yi: The first year of response that can be covered may include, but is not limited to, fixed, preset and/or dynamically variable devices, power supplies and any other components designed to ensure that such components are Or multiple control parameters to produce an action on a device (which may be mechanical electronic, magnetic, pneumatic, hydraulic, or a combination thereof). The processing element (which is associated with one or more response elements) that can be covered by the vaporization system

In this case, it means the extension of the material -

"real-time" action in the current or current state of the intention or process 12 200817501 Sex. Immediate actions may include (but are not limited to, factory, one process, one quantity, one calculation, one response, one response, -: 'one test response to one of the data taken, and the other, the device An action performed in a custom process in the system. The class can be related to the slow processing or characteristics of the second or minute or time ^ ^ in the system or during the time period. In terms of change, the process or characteristic that changes quickly is also related to one phase ί / ie, 1 亳 second, 1 〇亳 second '1 〇 (1 亳, 1 second) The same is true for the same term. The term "continuous" is used here. The device is either a normal implementation or an action performed at a certain rate or frequency. Including (but not limited to) a process, a repetition, a measurement, a calculation, a response, a data acquisition (via sensing elements), a device for the return ^ ^ clothing Xia Ma response _ capital # ^ ^ ^ ^ ^ ^ ^ τ ^ ^ ^ ^ ^ ^ ^ ^ ^ ^ t ^ t ^ ^ ^ ^ ^ ^ ^ ^ ^ ^ ^ # ^ Rate or frequency (times / second, times / minutes Sub-times, hours, etc.) are relatively slow-changing processes or features that are associated with a relatively faster process or characteristic (ie, 1 kHz, 100 Hz, 10 Hz, 1 Hz). In the present context, "reactant material" may refer to a feed or a partially treated or fully treated feed. In this context, "product gas composition (c〇 Mp0siti〇n 〇f the pr〇(juct gas)" refers to the entire composition of a chemical species in a gas. However, in practice, this term can be used to refer to the chemical composition of the most relevant for downstream applications. Concentration. For example, the gas composition required for a 01 iEL 4Λ emulsion turbine is usually expressed by the amount of nitrogen, carbon monoxide, carbon dioxide, water, and/or hydrogen contained in the system gas. It can also be indicated by the lack of a specific Chemical species (ie, do not wish to be transported downstream for t-valence, for example, 7 is very extensive when H2 is not included), depending on the feed, the composition of the feed, and the vaporization method used, then Gas cleaning and adjustment should be implemented. As a matter of course, the skilled artisan should understand that the gas composition may or may not cover the micro* elements. • - · · -. · . . . . . . . "Eharaeteristics gas" means the physical and/or chemical properties of a gas, which may include, but are not limited to, the chemical composition of the gas, temperature, pressure, flow rate, color, odor, etc. In this context, "escape" (off_gas) means a zenescent molecule produced by vaporization of a carbonaceous feedstock, which may include carbon monoxide, carbon dioxide, hydrogen, lighter hydrocarbons, and contaminating particles (eg, coal ash and carbon black p) "Syngas" refers to the gas product of the vaporization process, mainly containing carbon monoxide, carbon dioxide and hydrogen 'syngas can be produced by outgassing' or can be directly generated by the vaporization process (if the transition conditions allow this gas to be formed i For the purposes of the present invention, the term syngas herein refers to the product of the vaporization process' and may include, after addition to products such as decane and water, post-oxidation, carbon dioxide and hydrogen. The present invention provides a control system for converting carbonaceous to gas. In particular, the control system is designed to control one or more processes implemented in a vaporization system 14 200817501 and/or by one or more of its components to convert such feeds into gases, The gas can be reused in one or more downstream applications. The vaporization process controlled by the different examples of the disclosed control system can be various. The combination includes a converter, a residual reactor, a recuperator, and/or heat exchange. System, one or more gas regulators, a gas homogenization system and a wide range of applications. • . . . . . . . . . . . . . . . . . . Examples of these components and subsystems will be in the first!~][〇图..............._·· . _ . . · \ .. ' Detailed description, these illustrations come out Controlled by the control system of the present invention, .... . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . The control system can be operated to control various local, regional, and/or overall processes associated with the overall vaporization process to adjust various control parameters thereof; • . . . . . . . . . . . . . . Therefore, within or associated with the control system. * * .. - - · One or more components of the closure are provided with various sensing elements and response elements to capture various processing, reactants and/or product characteristics. The response is compared to an appropriate range of these characteristic values and implemented by one or more current processes (via one or more controllable processing elements). In one embodiment, the control system is used to control a vaporization process to convert the carbonaceous feed to a gas suitable for use in a selected downstream application. In one example, the vaporization process is controlled such that its gaseous product is ready for immediate use and/or immediate use. Thus, the control system can include, for example, one or more inductors to sense one or more characteristics of the gas to be applied to the downstream application. One or more computing platforms are communicatively linked to the sensing elements to access a characteristic value representative of the inductive characteristic, and the platform can be designed to define the characteristic value as a suitable gas for the selected downstream application. 15 200817501 A predetermined range comparison of such values for a volume, and calculating one or more process control parameters that can be performed to maintain the characteristic value within the predetermined range. Thus, . . . . . . . . is operable to link a plurality of response elements to one or more processing elements that are operable to affect the process and thereby adjust the induction of the gas: characteristics, and the communication link to the Calculate the platform to access the calculated: process control parameters and operate accordingly. · · · · · · · As a processing component. • · - ·. ... · . . . , * . For example, the control system can be used to control the conversion of a disc containing feed • · / ._·'· -- ... : . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . Used in a fuel cell to send electricity: electricity. In such applications, it is preferred to obtain the most efficient product that can be used as a fuel for individual generators. Or, if it is the feed of the product • . . . . . . . . . . . . . gas used in further chemical treatment, it will Become the most effective component of a specific synthetic application. In one embodiment, the control system provides process energy-feedback, feedforward, and/or predetermined to substantially maintain a reaction set point, thereby allowing the vaporization process to be performed under optimal reaction conditions to produce a predetermined composition Part of the gas. For example, a properly configured vaporization system can be used to determine and achieve the overall energy required to convert the feed into a gas, where various process characteristics can be evaluated and controlled to affect the net population. The decision of energy. Such characteristics may include, but are not limited to, the heating value and/or composition of the feed, the characteristics of the product gas (eg, heating value, temperature, pressure, flow, composition, carbon content, etc.), such characteristics The degree of change in the allowable value, input cost, and output cost. Various control parameters are continuously and/or instantaneously adjusted (which may include, but are not limited to, heat source power, additive feed rate (ie, oxygen, water vapor 16 200817501 gas, etc.)), feed feed rate (ie, one or Multiple unique and / or mixed feeds), gas and / or system Lili / flow regulator (ie, blower, release and / or control valve, kite), etc. 'Enable access and optimization according to design specifications Net overall energy b: • · '. · . . . . . . . . . . . . . . . . . . . . . . . . Or test, or in addition, the control system can be configured as an I system; the operation of the grain components to ensure proper operation, and selective, to ensure that the process implemented by the kg can meet the specifications Specifications. Depending on the implementation, the control system can be used to monitor and control the total energy impact of a vaporization system. For example, a vaporization system used to convert a feed can be minimized or minimized, or the one or more processes performed by the system can be minimized, or increased by these climbs. Waste heat recovery is achieved. Alternatively, or in addition, the control system can be configured to adjust the composition and/or other characteristics (eg, temperature, pressure, flow, etc.) of the product gases produced by the control system, and such characteristics are not only suitable for the mission. Downstream uses are also substantially optimized for effective and/or optimal use. For example, in a product gas system that is capable of driving a particular form of gas engine to generate electricity, the characteristics of the product gas can be adjusted such that these characteristics best match the optimal input characteristics of such engines. In one embodiment, the control system can be configured such that the entire vaporization process is such that it can meet the residence time limit or efficiency criteria for the reactants and/or products within the components, or can be consistent with the overall vaporization process Individual processing specifications and/or optimization. For example, in the implementation of municipal waste as a feedstock, the vaporization process for this type of waste is adjusted to compensate for the maximum retention time of the 2008-20081501 waste in the pre-treatment and/or the deposit period. It is very important to be (10). For example, waste and/or other feeds may be delivered to the control facility on a regular or continuous basis, where the disposal of such waste must be controlled to allow for continued operation (ie, to reduce or avoid downtime). , to prevent and avoid excessive accumulation (this will increase the retention during pre-processing, ... . . . - . time). In this type of real-world mode, the processing speed of a given feed can be controlled. _ · * /..··.· ..... ' . · · · · · Rate, depending on the quality of the fruit The feed rate, thereby allowing the transferred material to be stored or pre-processed: segments (ie, hours, days, or total t - a substantially constant residence time. .... . . . Similarly, it is possible to control the retention of the feed in a vaporization system converter. . . . . . . . . . . . . . . . . . . . . . . . . . . . Reduction and / or limitation. ' . . Downstream processing and / or application ) is fully processed 1 For example, a specific converter configuration can allow a fairly stable residence time to achieve appropriate processing Purpose (ie, within minutes or hours). It is also possible to control the downstream components of the converter so that the proper residence time can be substantially maintained. For example, sequentially arranging the gas through the heat exchanger, the adjustment system, or the homogenization system, These gases are optimized for a specific gas flow and/or residence time. Similarly, the town controls the components of such systems. Compensating and addressing variations in airflow and/or residence time. Those skilled in the art will appreciate that the vaporization system and control system 'in the various embodiments described above can be used in a variety of processing systems having separate and or combined plastic downstream applications. In this embodiment, the control system can control a process simultaneously by multiple directions in a continuous or immediate manner. 18 200817501 Control system architecture., ·, - . ', _ . ' ' - 参第13 And Figure 14, this control system can contain any type of control system architecture suitable for the current application. For example, this control system can include ... -.· ' _ . , 1 contains a substantial central control system (eg, Figure j3), a decentralized control system (Fig. I4), or a combination thereof. A central control system will generally comprise a central selection system that is configured to communicate with various local and/or remote sensing elements. : a bee; and a plurality of response elements arranged to sense the characteristics of the control process separately and via one or more controllable processing elements (which directly or indirectly affect the control process) return Should use. One of the centralization architectures' most of the calculations are implemented via a central processing unit, and the hardware and/or software that must be used to control the process must be in the same location. ; . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . The sensing and response components communicate and are responsive to local and/or regional processing components that are designed to affect a local process or sub-process. Communication between the decentralized controllers can be accomplished using various network settings, via a first control The sensor 14 senses the communication to a second controller in response, wherein the remote response will affect the characteristics sensed at the first location. For example, a downstream monitoring device can be utilized to sense the characteristics of the downstream product gas and adjust the control parameters associated with the converter (controlled by the upstream controller) to adjust the gas characteristics. In a decentralized architecture, control hardware and/or software are also distributed among the controllers, wherein a control module of the same, modular configuration can be implemented on each controller, or each control can be implemented. Implement various modular control on the device 19 2〇〇8175〇i

One other architecture, which is considered to be the scope of this disclosure, is separate but separate communication links. This type of architecture allows for local control along with other local control lines. Thereafter, the control subsystem communicates, or conventionally, the control system includes a plurality of response elements for controlling the reaction conditions and <<>> converting the carbonaceous feed to a chemical composition of the transition of the output gas and/or energy. In addition, the control system can determine and maintain operating conditions to achieve optimal, optimal vaporization reaction conditions. The ideal operating conditions are determined by the overall energy of the process, including factors such as carbonaceous feed components and products, gas specifications, and the like. The composition of the feed can range from substantially uniform to complete • ..... ..... uneven. When there is a change in the composition of the feed, it may be necessary to continuously adjust specific control parameters via the response element to maintain the desired operating conditions. * - · . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . And controlling the position of one or more heat sources of the vaporization system and the amount of power output, or controlling the extraction of by-products. The control system further includes a processing system (e.g., Figure 12). In an embodiment, the processing system can include a plurality of sub-processing systems. Referring to Figure 12, the control system includes one or more central, networked and 20 200817501 / or decentralized processors, one or more inputs (to receive the characteristics currently sensed by various sensing elements), and one Or multiple outputs (to communicate new or updated control parameters to the responsive response element. One or more of the control systems may also include one or more local and/or remote computer accessible media (ie 'RQM, RAM, detachable media, nose and media, etc.), used to store various preset and / or adjusted control parameters, set .... : * ... '·_ ·. · · . . . ' 疋 or better system and processing characteristics operating range, system monitoring and control 敕: · ... \ . * . Body, 搡 资 等于 is equal to it. Or, 芩· ..... .. *. . . Access to plasma decontamination process simulation data and/or system parameter optimization and modeling components via various data storage devices, an exemplary embodiment reveals. * * · ' . . . . . . . . . which is understood in the U.S. Patent No. 6,81,388, can be easily applied to the present invention. Some of the different platforms may also be equipped with one or more optional additional graphical user interfaces and wheeled perimeters to provide management access to the control system (including system upgrades, quasi-repair, modifications, adaptation to new system modules and/or Or equipment, etc., and various optional additional output peripherals for communication of data and information with external resources (ie, data machines, network connections, printers, etc.) .. . . . ······· As shown in this figure, this can be further enhanced by interactively executing various systems and/or processing beta ten calculations (which are defined to reflect the current state of implementation of a given vaporization system). Control system. Such calculations can be used in a variety of systems and/or processes, and can use simulation and control parameters of process and or system characteristics in a predictive and/or corrective manner to control the modeling. U.S. Patent No. 6,8, No. 388, which provides an example of such a system module that can be used with this control system to define various operations 21 200817501

The parameters and the prediction results obtained from this are the starting points for the various processes for implementing this system. In one embodiment, these and other such models are used occasionally or periodically to continuously re-evaluate and/or update various system operating ranges and/or system parameters. In the implementation, the NRC HYSYS simulation platform is used, and one input and the type of waste, any type of input: ..... * · ..... ... * ; . Academic composition, thermochemical properties, moisture content, feed rate, materials, etc.: consideration. This model also allows for the optimal selection of processes for selective use, such as location and feed type specifications, maximum energy recovery, minimum emissions, minimum cost, and cost. Finally, depending on the model selection chosen, this model can provide, for example, various operational characteristics, yields, system design characteristics, product gas transfer, emissions, recoverable energy, recyclable by-products, and optimally low Cost design, skilled artisans should be able to understand that ... + · . . . . . . * * Various representative examples of the US Patent No. 6,8 1 7,3 88 can be used in the present invention. ./ • . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . Can include any combination of no or less: proportional (P), integral (1) or differential (7) difficult to make 'for example control.. ..

Controller, I-controller, PI_controller, PD-controller, PID controller, etc. Those skilled in the art should be able to understand the ideals of p,] and D controllers depending on the following factors: the dynamics and delay time of the process part of the vaporization system, and the combination The range of operating conditions to be controlled, and the dynamics and delay time of the controller's combination. When adjusting a different control variable or control parameter from a point to a specific value, the important point when designing the controller combination can be short. The instantaneous period 22 200817501 and there is very little earthquake during the transition period. Those skilled in the art will be able to understand that these components can be implemented via a sensing element on a type of body that can be continuously monitored and compared to a particular value to affect the individual control elements. The reaction element is appropriately adjusted to reduce the difference between the target value and the specific explicit:: value. ' .. .1 . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . It is a well-known skill in this field. The combination of Ρ, I, and D is used in feedforward and feedback control programs. When correcting a good or feedback control-control parameter or control variable, the system is monitored by the appropriate sensing element and compared with a clear numerical range. A control signal is determined based on the deviation between the two values and supplied to a control element to reduce the deviation. For example, when the output gas exceeds a predetermined Kb:CO ratio, a feedback control member can appropriately adjust one of the input variables, for example, increase the amount of oxygen added to restore the Η2:CO ratio to the specified The value 延迟 is the delay time required to cause a control parameter or control variable to change via an appropriate response element, sometimes referred to as a "loop time." This loop time, for example, is used to adjust the power of the plasma heat source, the pressure in the system, the input rate of the carbon-rich additive, or the gas or vapor flow rate, which can be as long as 3 〇 to 60 seconds. In one embodiment, the product gas composition is a specified value for comparison in the feedback control program described above, wherein the amounts of C〇 and H2 in the product gas have been specifically specified. In another embodiment, the specified value is a fixed value (or a fixed range) β for the product gas heating value (ie, low hea value; ing value (LHV)) 23 200817501 Seven kinds of control variables and control parameters that require direct monitoring or model prediction are sufficient feedback control. Control variables and control parameters for a variety of vaporization systems can be used in the feedback control program. The pair can be directly or indirectly sensed and/or derived from the sensed value and controlled by the response to the strange action (use: adjusted control parameters > poor, the repair procedure can be effectively implemented in the control system to operate ^作

Multiple processing elements to make these characteristic values valid β: ........... ' . . . It is known that the traditional 'return or response control system can be modified to include a moderately variable and/or Predictive component in which a response to a given condition can be tailored to the response of the model and/or the previously monitored response to provide a reactive response to a sensed characteristic while permitting The compensation action is not ^^ ώ ϋ t ^® . ^ ^ 4, m ^ ^ ^ ^ ^ ^ ^ ^ ^ ^ The required data of the system and / Li history (four), x x Bu Yang / or the process characteristics sensed The response is that one of the previously monitored optimal values is ^ ^ ^ it ^ ^ ^ ^ ^ ^ flJ ^ # ^ 〇 ^ ^ ^ ^ ^ ^ ^ ^ χ does not deviate from the disclosure of the present invention. Under the control, the input parameters of the feed control process can affect the control variable i and the control parameters. The vaporization system can use feedforward control over a variety of control parameters, for example, the amount of power that needs to be supplied to one or more of the plasma heat sources. There are many different ways to control the electrical output of the plasma heat source arc, for example: with pulses Module current (which is supplied to the flashlight to maintain the arc), change the distance between the electrodes, limit the current of the flashlight, or affect the composition of the electric... 24 200817501 and location. Can be fed forward, using specific control elements to control the temperature or pressure of those additives that are modified in a gaseous or liquid state or in powder form or that can be sprayed or injected via a nozzle to the converter. And closed Olympus feed control ^: can be used in feedforward and feedback control · shoe order. Type control. The control of these profiles can deviate substantially from the typical p-combination control, causing the plasma 耝 reaction _ mechanics to be depleted by the model and constructing how to change the input variables or wheeling parameters to affect a particular result. Fuzzy logic control usually only needs to provide fuzzy and experimental interpolation for the reaction dynamics (generally the operating conditions of the system). The characteristics and implementation of fuzzy logic control and other types of control are well known in the art. : It is well known to those skilled in the art. It is to be understood that the embodiments described below are merely exemplary and that various changes may be made thereto. These and future possible variations are considered to be the scope of the present invention. And these changes are easily understood by those skilled in the art and are covered by the scope of the present invention. ^^_Control Summary As mentioned above, the control system includes a plurality of sensing elements for sensing one or the evening ' and / or system characteristics (eg, gas composition (0 / 〇 C 〇, 〇 / 〇 c 〇 2, 〇 / 〇 h2 荨), gas temperature, gas flow rate, etc.) and produce a characteristic value from the induced characteristics And one or more computing platforms for collecting and analyzing the values generated from the sensing elements and outputting appropriate control parameters to the one or more response elements 'which are arranged to be based on the inputs The control parameters are used to control one or more of the 2008 17501 processing devices y .., . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . (or selectively through the vaporization system) the gas flow and gas composition (whether in any natural variation using different types of plastic feed composition or similar feed sources), still in the pre-existing valley tolerance range to get the most Good gas storage and system by-products (commercial synthesis gas, recovery I body ^.......................) must recognize and make necessary adjustments to compensate for this type of Change. Monitor product gas parameters such as temperature, rate of extinction and composition, and change the relevant processing device: ......... · · · · · ..., . The characteristics of the product gas of the tolerance range (determined by the end use of the synthesizer body) are set. . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . One or . · : · · · · * , - . . . . . . .. Multi-flow rate, temperature and product gas composition to provide correction feedback, one-on-one or More of this carbon-containing feed input rate, oxygen input rate, vapor flow input rate, ..... · · · rate, rich in enthalpy additive input rate and the amount of power supplied to the plasma heating source to make corrections. These adjustments are based on changes measured in flow rate, temperature, and/or product gas groups, in order to ensure that these values remain within acceptable limits. 9 In general, the selected flow rate , temperature and/or product gas composition, must be optimized for the manufacture of gases with specific downstream uses. In one embodiment, the control system of the present invention simultaneously uses the controllability of plasma heat to drive the vaporization process, It also ensures that the airflow from the process is maintained within an acceptable range, even if there is a natural change in the composition of the division. In another embodiment, the control system of the present invention allows the total amount of carbon processed per unit time to be maintained at a fixed value as much as possible, and uses the heat of the plasma to determine the total amount of heat that enters and leaves the converter at the time of 2008. It is kept in the processing park. In other embodiments, the control system can also be adjusted, for example, to adjust the input air or gas flow in response to flow/pressure changes and/or . . . . . . . . . . . . . Any change in the gas plus V heat value: V This control system can also be set to + ..... _ . . . . . . . , . . . control, and / or adjustment occurs through either of the following The treatment, including solid residue. ... : ..., . - - . . Remaining adjuster, turn: gas adjustment t system, as shown in the figure. In general, the vaporization process of the controlled thorn of the present invention generally occurs in a conversion process, and the converter comprises one or more treatment zones and one or more heat sources, which can

And/or devices, and one or more plasma heating sources used to add ‘Wanwu. The conversion is to input one or more feed feeders fed to the converter and to add _ _ _ _ _ _ _ _ _ _ _

In one embodiment, the control of the reaction environment can be awesome from the converter 27 200817501 ^ ^ a ^ ^ ^ ^ ^ ^ ^ ^ ^ ^ ^ ^ ^ ^ ^. The control system can also provide means for controlling the total amount of feed, vapor, oxygen, and/or carbon rich material feedstock fed into the converter. Also &# τ .Π α „ ^ ^ ^ ^ ^ ^ ^ ^ ^ ^ ^ ^ ^ # ? It includes (but is not limited to) feed feed rate, additive feed rate, induced start blower to maintain ten The specific power of the Thunder 乂 乂 (1) power 篁, electricity to the power of the heating source and the emperor. The following will be detailed for each parameter. In an embodiment of the present invention, the plasma heat (for example, via electricity) The plasma heat source generated by the slurry torch or the like and the added additives (for example, vapor and/or oxygen and/or carbon-rich materials) help to control gas characteristics such as flow rate, temperature, pressure and The vaporization system can also use electrothermal heat to provide the required high temperature heat to vaporize the feed, recombine the bad gas produced by it, and/or ash the byproduct ash and convert it into Commercially available glass-like products. i + The vaporization process controlled by the present invention may further comprise a process for managing and controlling the solid by-products of the vaporization process. In particular, the first vaporization system may include a solid residue conditioner To convert from feed_to_energy The solid by-products or residues produced are converted into a smoothed homogeneous material having a low leakage property. The solid by-product form of the vaporization process may be coke, ash, slag or a combination thereof. The solid residue conditioner may comprise a solid residue conditioning chamber to or region, a plasma heating member or other such heating member (which is adapted to provide sufficient high temperature), a slag wheeling member, and a control member (which Department can operate 28 200817501 to link to the overall control system of the 飞w m 介 》 》 》 》 》 》 》 》 》 》 》 》 》 》 》 》 》 》 》 》 》 》 》 》 》 》 》 》 》 》 》 》 》 》 》 》 》 》 》 》 Forming a compact 矽> section, when the ore metallic glass material is poured from the processing chamber or region, it is cooled to become a tight metallic, non-exposed dream metallic solid slag. Two _ ^ ^ ^ ^ &, the disclosed control system is adapted to make M ^ ^ ^ ^ V in the SRC; ^ ^ it ^ ± m ^ ^ f # « : 〇; The vaporization process controlled by the present invention Also included is ^ ^ ^ ^ m Μ ^ ^ ^ ^ Μ ^ -Λ It: The exchanger) is used to perform this:: The same type of flow is used to heat the workers. After raising or other oxidants (for example, 氡I), these gases can be used to provide heat to the vaporization process, and the recovered heat can also be used. For industrial heating purposes, or to control one or more steam generators, as part of a vaporization release that can be used as vaporization and/or recombination reactions. Additives, or used to drive a steam engine for power generation. In addition, as shown in Figures 24-25, the heat exchanger can also include additional heat exchangers that can operate these additional heat exchangers from various other systems. Thermal energy is extracted from components and processes, such as via a paddle heat source cooling process, a melt-cooling and processing process, a converter gas regulator cooling process, and the like. The control system of the present invention may also include a control subsystem for controlling the heat recovery system operatively coupled to the overall control system of the system to optimize the overall heat transfer of the vaporization system (see paragraph 15). And 16 6)). The vaporization process controlled by the present invention may further include a northerly gas adjustment 29 200817501

Intensive-GCS- (see Figure 1-1, and Figure 29, Figure 59_6) or other such gas conditioning components to adjust the product gas available for downstream applications from this vaporization process. . For example, the product gas can be directed to a rod> (匕器: Ning body adjuster, as described above, can be self-processed to talk about the residual gas in the residue of the dancer): The treatment step is applied to produce an output gas product suitable for downstream use.: In the embodiment, the converter gas is adjusted: the whole step is reversed, for example, from syngas| Through a bag filter, cyclone or the like), pity gas (HC1., ' . . . . . . . . . * * · * ': HzS) and / or heavy metals, or adjust these When the gas passes through the vaporization system... · · , · · Degree and temperature. The processing sequence consists of synthesis gas and is available for downstream applications.

The specific composition of the output gas determines that the 9' gas adjustment system can also include a control system that is operatively coupled to the overall control system to optimize the converter gas adjustment process (see Figure 1 5-1 6) ). The vaporization system controlled by the present invention may further comprise a gas homogenization system for providing at least a first stage homogenization of the product gas. For example, the product gas can be left in the homogeneous system for a specific residence time, so that the various gas characteristics are at least partially homogenized to reduce variations in such characteristic values. For example, the chemical composition of other specific product gases such as force and/or temperature and such as flow rate, dustiness may be at least partially stabilized by a homogeneous system to achieve downstream standard high for downstream applications (eg, gas properties) Stability. Therefore, a homogenization system can be used to help lift gas turbines or engines, fuel cell applications, etc.) In one embodiment, the homogenization system of the vaporization system provides a gas 30 200817501, a meandering L to or the like, the size of which can be A gas residence time sufficient to achieve a sufficiently consistent turn-off composition, pressure, temperature, and/or flow rate is accommodated. In general, the characteristics of the homogeneous system will be specified based on the criteria for downstream use and the capacity of the control system to reduce variations in product gas property values. > In Section 5-1, any person skilled in the art will understand that the control system....; . . . . . . . . . . . . . . . . . . . . . . . . . . . It can be used in several systems that produce energy and . . . , 'transformation (which has numerous independent and y or combined downstream uses). Lifting ... ... -··,. ,. · · : . . . ' ' ..... . " '..·.· ' ' For example, in the embodiment of Figure 5 An integrated gasification combined cycle (IGCC) system can be used to provide a syngas (which can be used for one or more gas engines) and steam. * - ' ' . - (Using one or more heat exchangers to cool the synthetic fluorine produced by the outgas associated with the gas engine) to produce an output energy for use in one or more steam engines. In the embodiment shown in Fig. 6, the control system can be used to control the .. - '. · · · · a vaporization system that combines an integrated vaporization group cycle (IGCC) system and A solid. Oxide fuel cell system, the latter is used. One of the syngas is rich. · ····· _ , . : Hydrogen-containing to the stock, to produce energy (ie, power generation). In the embodiment shown in Figure 7, the control system can be used to control a vaporization system that combines an integrated vaporization combined cycle (IGCC) system with a molten % acid 8 曰 fuel cell system, the latter being as in the sixth In the manner of the figure, one of the hydrogen-rich by-products of the syngas is also used to generate energy (i.e., generate electricity). In the embodiment illustrated in Figure 8, the control system can be used to control a vaporization system that combines a solid oxide fuel cell system (e.g., No. 6.31 200817501 and/or multiple steam engines) The steam generated by the heat exchange of one or more steam generators from the synthesis gas and the output of the fuel cell in a cocurrent flow recovery manner is initiated by .. . . . . . In the illustrated embodiment, a permanent vapor shift converter is added to the embodiment of Fig. 8 to provide an enrichment that can be used in the solid oxide fuel: battery system; The illustrated battery system replaces the solid oxygen of Fig. 9 . . . . . . . . . . . . . . . . The embodiments of the present invention are not exhaustive, and any one skilled in the art will understand that the disclosed embodiments may be modified or modified without departing from the spirit of the invention. Can be applied in other situations. - · - - . . Refer to Figures 15, 16 as As described, the control system 8 can be integrated into a particular vaporization system 10 to monitor various systems via a plurality of sensing elements 2 〇 2 . . . . . . . . . . . . . . . . Most of the response elements 206 perform various trimmings to control parameters to manage energy and maintain each characteristic of the process in a particular tolerance. These parameters (discussed in detail below) may be derived from one or more plasma converters. 100. Solid residue conditioner 400, plasma heat source 150, and slag processing heat source 450, heat exchanger (ie, gas-to-air exchanger 5〇0 and/or steam generator heat exchanger 599) In the process, and additive inputs, primary and/or secondary feed inputs (ie, carbon rich additives (HCF)) associated with the processes, converter gas regulator 600, homogenization system 700, and any other Modules for processing components or vaporization systems 32 200817501 .. group, . ' . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . Device (one or more computing platforms of the control system) to store Most of the predetermined and/or re-adjusted system parameters are: 撮: for data and (option or system simplification and modeling components, this control system can more system interaction, so that the system round 1 product gas composition { · . · ...... ...... One or more characteristics in the preset range of the factory as mentioned above, if the production of gas is prepared in the 'electric system 丨The product of the fuel of defeat. _ ' .. · ' - · ' . : . * · · The main component of the output gas leaving the converter can be used in the vaporization process controllable by the control system of the present invention, which is mainly an oxidation barrier, two Oxygen two carbons ^ Hydrogen and steam, and a small amount of nitrogen, which may also contain a smaller amount of methyl, acetylene and hydrogen sulfide. The ratio of widely oxidized carbon or carbon dioxide in the output gas (depending on the amount of oxygen in the converter), for example, when the oxygen flow rate is controlled to exclude the conversion of carbon to carbon dioxide and carbon monoxide. The metering ratio, the process operation will primarily produce carbon monoxide. The composition of the product syngas can be optimized for a particular application (eg, a gas engine and/or a fuel cell for power generation), such as by adjustment The equilibrium relationship between plasma heat, oxygen and/or steam and/or carbon-rich additives. Since the addition of oxidant and/or steam additives during the vaporization process affects the chemical reaction during conversion, the control system of the present invention is preferably The sensing element can be monitored to monitor the composition of the syngas. The input of the reactants can be modified via the responsive element to maintain the characteristic value of the syngas within a predetermined range suitable for the selected downstream application. ·,..... . . . . . . . . . . * can be used as various types of sensing elements (such as 'nature body composition lean sensing element, gas flow sensing element, gas dust force Should:: Yuan to monitor the product to determine the hydrogen in the synthesis gas V - oxidation ^ 〆 synthesis gas, the special nuclear value for various, the figure is not implemented) are very useful. The composition of the product gas is generally in * ' · · .'. '. ··; ' . . . ; , After the gas has cooled and after the adjustment of the removable particulate matter, the process is finished. . . . . . . . . . . . . · · ' .. . measured, although this measurement is too much to sample and fractionate the product gas by conventional methods. One of the methods that can be used to determine the chemical composition of the product gas is gas chromatography (gas chromatography ( GC) analysis). The sampling points for these analyses can be integers. -. .. .; . . . . In one embodiment, the gas composition price is measured by a measurable gas of .. . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . In one embodiment, the sensing element at the exit of the angle converter is used to monitor product gas characteristics, such as temperature, flow rate, and composition. In another embodiment, the sampling gas is installed in the product gas. Anywhere in the processing system. As described above, the response element is set to change the input reactant to maintain the characteristic value of the product gas within a preset range suitable for the selected downstream application. Features of the invention also include utilizing the composition of the determined output gas stream. And adjust the process to determine if too much or too little oxygen is added to the vaporization process. 34 200817501 In a common practice, use an analyzer, sensor or other such sensing element to measure the relevant characteristics in a carbon monoxide gas stream. Value, for example, a list of concentrations such as carbon monoxide or other suitable oxygen-rich reference material. • . . . . . . . . . . . . . . . . . . . . . . . No main raw i carbon. In another embodiment, the ratio of carbon dioxide to carbon monoxide is in the other. In another kind of control game @ use the inductor to determine the underlying concentration of the electropolymer generator It is assumed that one or more process control parameters in the range and the components are used to influence the process and adjust the special values. In one embodiment, the values of C 〇 2 and H 2 are compared and compared with the value or range of 镡. In another real method, the product gas heating value (ie, LHV) is measured and compared with the value or range of the target, as detailed below. . . . . . . . . . . . ..... . . . . : : A person skilled in the art will be able to understand the measurement of these and other product gas characteristics, which can be implemented by the specific system described above or by other such sensing elements via the response element to monitor and adjust the current The process is performed to maintain the product gas characteristic value within an appropriate predetermined range, and is not limited to the above described embodiments and the illustrated system and the control system shown in the drawings. Temperatures at various locations within the system -- --------- " ----- In the implementation of this month a month A component (eg, an inductive component) that monitors the temperature of each location of the system is provided and collected in a continuous or intermittent manner. The sensing component suitable for monitoring the temperature of the converter used in the control system can be placed in the converter. Exterior wall, or at the top, center and bottom of the converter in the refractory. 35 200817501 Inductive components for monitoring the temperature of the product gas can stand at the product gas outlet and throughout the product gas conditioning system (also That is, a gas regulator in the converter). Multiple thermocouples can be used to monitor the 阙: degree of the 阙 key position around the roundabout converter? · ······. . . . . -. * *' ... - ·- ' : ...- · . . . . . . . . . . ' . . . . . . . . . ' If you use a recyclable vaporization system (f column such as 'one parent replacement or gas collection system: after the temperature can be used gas-to-air heat exchanger, airflow generator or both for recovery The thermo-oxidant produced by the chemical process uses a heat exchanger embodiment to set the temperature transmitter to measure the temperature of the gas and gas at the outlet and inlet of the helium exchanger. A temperature transmitter can also be set to measure the refrigerant. Rope after heating in heat exchange pain: .. ' . . . .... ;; · The control system can use these temperature measurements to ensure access to individual heat, the product gas temperature is in For example, in an embodiment, if a gas_to-air heat exchanger is designed to have a temperature of 1050^, it can be used in a heat exchange, gas enthalpy, L. The medium-sensing transmitter controls both the refrigerant air flow rate and the slurry heat through the system to maintain the optimum product gas temperature. The exit temperature of the object body ensures that an optimum amount of induction heat has been recovered from each heat recovery stage of the product gas. A temperature transmitter installed in the air outlet stream measures the temperature of the heated heat exchange thief-air to ensure the process It has been carried out under conditions that ensure that the process air is heated to a temperature suitable for vaporization. In one embodiment, the 'cold coal air exits D temperature is about 65 ° C, so the temperature is transmitted at the air outlet stream 36 200817501. The data can be provided, and the data can be used to determine whether or not to adjust. -. ..... .. Through one or two of the air flow rate of the entire system and the power of the electro-converter. ... to ensure that the optimum product gas input temperature can be maintained, which can be used again..... ... ... ... controlling the temperature of the refrigerant air. For those skilled in the art, For any of the processes... The temperature adjustments made by the subsystem are not determined solely by the optimization of the particular subsystem, but also the needs of the downstream application. For example, when controlling a specific In the local and / or regional process, the overall needs need to be included According to one embodiment, wherein the vaporization system used with the control system of the present invention comprises a steam generator heat exchanger, the control strategy sets a fixed point for the optimum refrigerant air temperature, for example, about 60X: and is produced by steam. . . . . . . . . . . . . . . . . The gas leaving temperature of the heat exchanger is set to a fixed value, for example, about... * . . . . * 2 3 5 ° C. Therefore, according to this embodiment, when the product gas flow is reduced, the temperature of the product gas at the outlet of the gas-to-air heat exchanger is changed. Cold, thus reducing airflow generation, because the gas exit temperature of the steam generator heat exchanger is also set at a fixed value. , * . * . · * · This concept also applies when the airflow is reduced through the system. According to an embodiment of the present invention, since the temperature of the leaving refrigerant air is fixed, because of the difference, the differential gas exiting from the steam generator heat exchanger The temperature is hotter so more steam can be produced in the steam generator heat exchanger. However, as the flow through the system is reduced, the product gas flow is also reduced, thus increasing the temperature entering the steam generator heat exchanger with only a temporary increase. For example, if the airflow is reduced by 50%, the steam generator heat exchanger will temporarily treat the highest inlet temperature as 800 °C, which is within the temperature range of the heat exchanger design. 37 200817501 In an embodiment of the invention, the thermal light installed throughout the system is used as an induction element to provide the required temperature monitoring. Thereafter, as described above, the control system can use these temperature measurements. Those skilled in the art will be able to understand the temperature measurements performed by the above-described and other such inductive elements in a particular embodiment of the system, which can be

The preparation of the ginseng: to produce a product oxygen suitable for the downstream enthalpy, and to select the volatility and the efficiency of the ^ and its control is not limited to the pressure of the control member V system as shown in the diagram. In one embodiment of the invention, the entire vaporization force is used in the sensing element t and in conjunction with the present control system, and these data are collected in a continuous or intermittent manner - in still further embodiments, these pressure sensing elements include A pressure sensor (eg, a pressure transducer) located on the wall of an upright converter. The control system uses these teachings related to system pressure to instantly determine whether to adjust parameters such as plasma heat source power or feed rate or additive rate. ... - Winter changes in the amount of vaporized feed will result in rapid vaporization, resulting in significant changes in the pressure in the converter. For example, if the amount of feed introduced into the converter increases, the pressure inside the converter will rise rapidly. . In this case, it is preferred to continuously monitor the pressure using the sensing element to provide the instantaneous data required for the adjustment, and to process the control parameters (eg, the pressure of the induced blower) via the response element to reduce the system pressure (in the converter) The pressure value measured at the inner and the inlet of the converter locks. Another pressure sensing element can be selectively used with the solid residue regulator and operatively connected to a control valve to guide 38 200817501 ^ from solid a solid residue regulator gas of the residue regulator to the ammonia regulator. Another pressure sensing element is selectively operably coupled to the homogenizing system to the control valve for passage through the high stack The steamer flows to the converter to maintain the continuous operation of the gas engine. The flow sensor can also be used throughout the system. The speed of the vehicle is measured. ..... . . . . . . . Further ^ ^ ^ ^ pressure drop of individual components, in order to pre-empt the execution of aunts and mothers.... : 隹 隹 隹 此 此 此 此 此 此 此 此 此 此 此 找到 找到 找到 找到 找到 找到 找到 找到 找到 找到 找到 找到 找到 找到 找到 找到 。 。 。 。 。 。 。 。 sweet Health 7 / Solution I from the above and other such inductive meta-casts [Shenzhen implementations use the above and other system force monitoring and control ^ ^ ^ ^ ^ ^ ^ ^ ^ ^ ^ ^ & ^ ^ ^ ^ ^ ^ ^ ^ ^ ', ° product oxygen for downstream application, and selectively optimize process V output and efficiency, and it is not limited to the above-mentioned coveted control members. This thin mode and the * shown in the drawing, _ . • - * ' - . In the virtual I flow rate implementation, the control system includes sensing components to collect these data in a whole # or batch mode. ^The gas flow rate through different components of the system will affect the 敎 component The gas flow rate of the recombination area is too large, and the composition of the milk may not be sufficient when it reaches the balance, resulting in a non-optimal 39 200817501 vaporization process. The above and other gas flow years are located in various embodiments of the system. The measurement and control component can monitor and adjust the process currently being performed via the response component to generate a product gas suitable for downstream applications, and selectively optimize process output and efficiency, and is not limited to The embodiment described above Control member shown in the drawing.:: Process Promoter ^ .. :: .· : : . . - ' . · * ' . * : . : ' ;:; ..... · Can contain - Or, please ^ ^ II (ref〇rme〇^, b, ^ # ^ ^ ^器 can also include the handling of W, such as the approval of this conversion / ground device such as feed wheeled components for feeding For feeds, the feed may include, for example, urban temple insects, sulfone flat solid waste (MSW), high post feed (hcf), msw, and HCF. Other processing means may include means for adding a volume of recordings (components of the additive, such as not limited to) steam, oxygen, air, and containing (reported). Air, oxidant and carbon Fengchang additives (the latter can be selected in the gender range; the product gas enthalpy value in one ^ ^ ^ can also contain one or more plasma heat V original, as in other sources of heat Know that m Μ 14: Wr ^ AAr and or the control unit can selectively operate the control of the thunder and 〆 浆 source. This hand can also provide 甩 to the input m匍〆蛀This conversion state can also be equipped with various kinds of t (inductors), such as thermocouples, and also for the slanting yam [force sensor, etc. The control system of the present invention, the dying of the quenching, the conversion, various characteristics Control, including (but not limited to 40 200817501) input, additives, Thunder: ^ ^ ^ ^ ^ ^ ^ ^ ^ ^ ^ ^, plasma power, waste height and hemp pass The movement of the converter. . / ^ ^ Λ * . . _ ;. ..·.'. · .' · The converter can have a wide range a 丄^ % day 7 length-to-height ratio, and the direction A can be upright or horizontal 々 ^ ^ ^ ^ ^ ^ ^ ^ ^ ^ ^ ^, ▲ 地. This converter will have -- or more than hell The combination 1 depends on the outlet set at a certain part of the bottom of the chamber to eclipse the lacquer, so that the residue can be discharged by gravity flow. In an embodiment, Φ, 1 fi 侔 白 white drum 枳 卜Eight of this converter will make the physical transfer structure ^ ^ # ^ ^ ^ ^ Λ _ @ ^ 〇 ^ ^ ^ ^ ^ ^ T ^ t # 4 0 M ^ ^ ^ can also be vaporized (see Figure 22 Processing in the same chamber, or in another chamber different from the chamber in which vaporization is performed, as shown in Fig. 23. ... ' * * .... ...: ' ' : . . . . ...................::: In an embodiment of the invention, the one or more plasma heat has a conversion process for the feed_to_gas In an embodiment, combining one or more plasma heat sources with input steam and/or oxygen additives helps control the gas. ·'.:..·' ..... _. Body composition. Plasma heat can also be used to protect the outgas generated in the vaporization process (of Fgas) gas is completely (or mostly) rodized into its constituent elements, such that the constituent elements can be recombined into a product gas having a specific composition (for example, in a reformer different from or integrated in the vaporizer) This recombination may occur in the same region or chamber as vaporization, or in another unique region or chamber within the converter, referred to herein as a "ref〇rmer." Thereafter, the product gas exits the converter from one or more output gas outlets 41 200817501. : vaporization of the carbon feed (ie, 'converting the carbonaceous feed substantially into a synthesis gas) occurs in the converter and can be carried out at high or low temperatures, or at high or low pressure, The process of converting the carbon feed to syngas products is a reaction to the shoulder. : With the design of the carbon-containing feed in the γ, chemical and thermal aspects of the ^. .· :··♦_·.♦ ♦ . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . ' · ... : The V-containing carbon in the eliminator will be shaken: the moisture remaining in the keke will be removed by the ^^ / as the temperature of the dry feed increases, it will also open to cause thermal cracking. During thermal cracking, the volatile components are volatilized and the feed is thermally decomposed to release the char, benzene gamma. At the same time, the feed is also converted to char. Carbon contains residual solids composed of organic and inorganic materials. The carbon obtained can be reheated to ensure that its gas composition can be completely converted, JR; leaving behind ash by-products that can be converted to slag. In one embodiment, the vaporization that hinders the feed is carried out with a controlled amount of oxygen, which may also be selectively controlled under the control of the control system of the present invention to minimize the amount of burn. A combination of drying, volatilization and carbon-to-ash conversion steps provides an intermediate outgassing product. Further heating (generally under one or more electric heat sources and under a controlled amount of additives (air and steam)) this intermediate outgassing product can further convert the carbon-containing feed to a synthesis gas c/this step Also known as a "reformulation" step, it can occur in a chamber that is the same or different from the vaporization process, that is, in an integrated or different vaporizer / 42 200817501 reformer. · · ··· . . . . . . . . : The position of the one or more electrical heat sources is such that all reactions occur simultaneously or the multi-plasma heat source is placed in the converter These reactions occur sequentially. Regardless of the two types of parenting staff; the η* ritual recognition method will increase the thermal cracking temperature because of the eight plasma sources in the converter. · ····**.· . . . . . . . . . . . . . . . . . . . ( ( ( ( ( ( ( ( ( ( ( ( ( ( ( ( ( ( ( ( ( ( ( ( ( ( ( ( ( ( ( ( ( ( ( ( ( ( ( ( ( ( ( ( ( ( ( ( ( ( ( ( ( ( ( ( ( ( ( ( ( ( Avoid burning the feed in the converter and avoid diluting the product gas with nitrogen and excess co2. . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . A single-stage or multi-stage conversion process is available for the various exemplary converter designs. See WO/2006/128285 and WO/2 006/128286, the disclosure of which is hereby incorporated herein by reference. .... V . . . . * . . . The skilled person understands that in an example the 'transformer design system is used for . . . . . . . . . . . . . . . . . . . . . . . . The process of gas can occur in the processing of a single section, and also . . . . . . . . . . . . , ie, vaporization (turning the feed into outgassing) and recombination (will The gas becomes syngas. The process can be carried out in another instance of the system. The other '. . . -- converter design system converts the feed into syngas Process occurs in more than one area The process can occur in more than one region of a chamber (i.e., embodiments of Figures 20 and 22 can be interpreted as representing a multi-zone, single chamber converter), more than one region of different chambers (i.e., the embodiment of Fig. 23) or a combination thereof, wherein the regions are in flow communication with each other. The converter may optionally include one or more progressive processing devices, Example 43 200817501 ·· _ . . . . . . . . As an additive input member, it is possible to add a gas such as oxygen, air, oxygen-enriched air, steam or other gas that contributes to the vaporization process to the converter. The article may also be provided for inputting a carbon-rich additive into the converter, and the agricultural-rich additive may also be supplied by a secondary feed input member, for example: Figure 19_23 defines a string of seed treatment devices It consists of a mixed feed John component, which shows the combination of the main feed input rubber and the two feed intrusion members of the selection front. The components may also include air (or oxygen) input 埠 and / Or 篆汽翰 into the bee and the factory or rich The culprits are filled with sputum, which is selectively supplied via secondary (or mixed) sputum selection. These openings in the converter allow the distribution of additives in the converter to reach the final 隹 AV- 〇«fc J. *JL. j, 方式 The way in which the bite is added to the sputum cloth plus the additive will be described in detail below. ♦ * · .... . . . . . . . * . ' . . ' . Carbon-rich additives (or secondary feeds, /, k ^ , * human needles) can be any carbon source material that can be added to the vaporization $ %, D/Fly The chemistry is introduced to provide the available carbon content in the vaporization process. The use of carbon-rich 驻 驻 驻 丄 丄 丄 材料 材料 材料 有 有 有 有 有 有 有 有 有 有 有 有 有 有 有 有 有 有 有 有 有 有 有 有 有 有 有 有 有 有 有 有Examples of additives that can be used to vaporize the manufacturing process include, but are not limited to, tires, plastics, advanced coal, or combinations thereof. Referring to the embodiment of Fig. 23, wherein the converter shown by the edge comprises a horizontal sonar converter, which is further divided into three vaporization zones to sequentially promote dry selection η ^ dry 4 in the parental region. The conversion step of volatilization and charcoal-to-ash (or carbon conversion) optimizes the process of extracting gaseous molecules from the carbon feed as above. This allows the feed to be dried under a specific temperature (ie, 300eC to 90CTC) by moving the feed from the first zone to the second zone. 44 200817501

Drying, in the second zone, the volatilization occurs in another temperature range (ie, 4〇〇〇c ～95〇1), and before moving into a third zone, in the third zone? - The ash conversion process (or Wei carbon conversion) occurs in another temperature range (ie, 6〇〇X~1000$). The ploughing process occurs at each stage of σ, roughly showing the employment of the 2nd and 7th 8th In the figure, and in detail in the following examples, the seven I ^ ^ ^ ^ ^ ^ should be based on the dioccupant area (which mainly refers to the dry release, better than the volatile deuteration process) 4 Completely dry and primarily carbon conversion process). The horizontal expansion of the vaporization process allows for the optimization of the vaporization process by regionally promoting the vaporization process or the multi-barrier to optimize the characteristics of the feed material at specific locations within the chaotic population. Any one skilled in the art will be able to ^ ^ T ^ ^ # ^ ^ ^ # , b ^ ^ ^ ^ ^ ^ ^ ^ ^ ^. The following discussion will describe the manner in which the conversion is divided into three steps. However, in the % 23 yoke mode, the movable material is supplied through the converter to promote the specific stage of the vaporization process, and the components of the external (inflammation, volatilization, and charcoal-to-ash) phases. The "2" process is also provided to control the movement of material through the conversion of the Han servant. One or more material transfer units can be used to facilitate the material movement. The material transfer member is moved by changing the movement distance and The movement of the material transfer members relative to each other, the material or the multi-material transfer member can be made in a coordinated manner. In order to optimize..., control, total residence time and material stack height in the chamber, 45 200817501 ·····' . · · . . . · · Different speeds ' different moving distances s丨丨: bK ϋ ^ ^ ^ ^ ^ Move the frequency while moving each individual material to the individual components. This material is transmitted from ^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^ Augers, shelves, platforms, hammers and other such components. Various examples of materials that can be used in the present invention are disclosed in the International Application No. WO/2006/12JO, which is incorporated herein by reference. For example, a water: flat pass member includes a plurality of horizontally transposed two soils, a dwarf, a multi-sister motor component, and a multi-view actuator, wherein each of the individual levels transmits alpha and a guiding element. The response light member can operate the transfer member through any of the conventional components (9), the hydraulic machine and the pneumatic machine. In an embodiment, a material transfer member is provided to move the MSW along the converter such that a suitable process can be performed at an appropriate stage within the converter: 'and the used residue can be Move to the solid material section of the converter. It is also possible to control the material stack height for each stage (platform) and the total retention span within the converter. These functions are controlled by a system of multiple load arms on each stage of the broken (platform) floor. Each carrier arm can move along the full or partial length of the stage (platform) and can also change its speed. This allows the material stack height and residence time to be controlled, and, if necessary, the platform can be completely emptied at this stage. The carrier arms can be a single carrier arm or multiple fingers. Power may be supplied by an electric motor to move the carrying arms, which may be driven via a gearbox and roller chain system. These motors are controlled by a control system that commands the start and stop position, movement speed and frequency of movement. Each carrier arm can be individually controlled. In the case of a real 46 200717501, a roller strip is used. This can withstand harsh environments. In the case of a real Λ 。 。 。 。 。 。 。 。 。 。 。 。 。 。 。 。 。 。 。 。 。 。 。 。 。 。 。 。 。 。 In another spring, each of the two chains of the carrying arm. The Straight 1 method can provide an external L-month degree from the recognition ratio without the use of precision guides. Following this V, the members are aligned with each other at an angle of the carrier arm. In order to avoid when carrying the arm: lower buckle /,: when retracted under the bearing r, the control system can be pre-set _ transfer "soil with: take the first move to the lowest carrying arm, you from the mountain JJL + :1 ^ α 乂 中 中 中 中 中 中 中 中 中 中 中 中 中 中 中 中 中 中 中 中 中 中 中 中 中 中 中 中 中 中 中 中 中 中 中 中 中 中 中 中 中 中 中 中 中 中 中 中 中 中 中 中 中 中 中 中 中 中 中 中 中 中 中 中 中 中 中 中 中 中 中 中 中 中 中 中 中 中 中 中 中 中 中 中 中 中 中 中 中 中 中 中 中 中 中 中 中 中 中Extending the gap behind the highest carrying arm, then retracting the central bearing 'by any gap in the feed 淳h, and then retracting from the control system from ^_ in one embodiment, using heat such as heat Coupled sensors to monitor the temperature of the converter. Temperature changes can be monitored along the points on each stage of the platform and at each level of each stage. The temperature is controlled by the hot cake = Periodic replacement is required during operation... In order to achieve this without shutting down the process, a sealed end tube can be used to insert each thermocouple into the earner, after which the sealed end tube is sealed within the converter housing. This design allows the use of longer elastic threads than sealed end tubes The thermocouple allows the junction surface (temperature sensing point) of the thermocouple to be pressed against the end of the sealing tube to ensure correct and fast response to temperature changes. The end of the sealing tube can be sealed to the converter and compressed Member (which can accommodate the protrusion adjustment into the rodifier) 47 200817501 #口持在疋位. When it is necessary to measure the temperature of the material pile, the Mixian will move when it is caused, the problem can be provided at the end of the sealed tube. You / 1 偏 偏 , , , MS MS MS MS MS MS MS MS MS MS MS MS MS MS MS MS MS MS MS MS MS MS MS MS MS MS MS MS MS MS MS MS MS MS MS MS MS MS MS MS MS MS MS MS MS MS MS Conversion ^ r

Shape: Mud: Poly, liquid, and gas materials are ploughed by agriculture or multiple inlets. The location of these inlets can provide the most entanglement; heat, so that the feed can be fully and effectively converted into Product gas brain-body 0 According to one embodiment of the invention, the wall of the converter is lined with refractory material. The igniting material may be a non-pressurized reaction material suitable for use in a converter at a high temperature (for example, between about , . . . , and between 11 〇〇C and 1400 ° C), Or a combination of various conventional refractory materials. Various exemplary converters and transformants are disclosed in detail in International Applications 荦 W〇/i〇〇6/128285 and WO/2006/128286. Any one skilled in the art will appreciate that by moving the one or more plasma heat sources, by adding other plasma heat sources, other heat sources, etc., the present invention will be described without departing from the general scope and disclosure of the present invention. The converter operates as a converter with a single processing zone or multiple processing zones. In fact, by monitoring the one or more direct or indirect processing characteristics associated with vaporization and/or formulation processes performed in a particular converter, regardless of these processes Is occurring in a single chamber or multi-chamber 48 200817501

The skilled artisan should understand that although the city secret Bn such as ω 2, a... converter class, set and its available sum .. .. · * * - ; . . . category: use other converter types

Also, the method of converting a carbonaceous feed to a hemp-producing gas uses one or more plasma heating members that can be controlled by the control system of the present invention to control the substantial conversion of the product gas to a desired product for downstream specific applications. An electrothermal heating member is selectively provided to heat the carbonaceous feed to drive the initial vaporization process. .... In one embodiment, the location of one or more plasma heat sources is optimized to allow the process of converting outgassing into a suitable product gas. According to the design of the vaporization process, the setting position of the one or more electric heat sources is selected, for example, according to whether the process adopts a one-stage platform or a two-stage platform vaporization process, whether there is one or more converters, and whether or not to re-form The device is integrally formed or separately present, or the converter is determined horizontally and/or uprightly. A variety of commercial electric heat sources for long-term high temperature use have been developed. In general, such plasma heat sources have output power sizes ranging from 100 kW to over 6 MW > X to produce the desired amount of conversion of outgas to syngas products, for example, more than about 9 Torr (rc to about 11). 〇(temperature of rc. 49 200817501 Embodiments may include an inductively-fitted electric torch (Icp), (iv) and a non-transporting electric arc torch (both DC and AC). It is a technique well known to those skilled in the art. % Λ ^ ^ # ^ ^ Λ7 ^ Λ ^;^ ^ ^ ^ ^ can be injected into the electrical discharge path of the plasma heating source: In the implementation of the early step:七 ^ ^ ' ϋ ^ ^ ^ ^ ^ ^ ^ ? mm; M% is operated to adjust its position and date. ' · · · · · · ' : · . ' · ' * :,, ··· * In the Known Way, the 'this gasification process uses the controllability of the electric heat collection' to drive the conversion process and ensure that the gas flow and gas composition from the converter remain within the preset range. Control of plasma heat also Helping the body, regardless of whether the composition of the cerium-containing feed is different or whether its source is subject to change. In one embodiment, the control system of the present invention comprises The component is used to adjust the power of the plasma heat source to manage the net total energy of the reaction. In order to manage the energy required for the reaction, the power supplied to the plasma heat source can be adjusted to maintain the temperature of the vaporization system constant, regardless of the feed composition. The variation is a change in the relative feed rate of the vapor, air, and/or carbon-rich additive, and in one embodiment, the rate at which the control system can be introduced into the converter, such as the carbonaceous feed and the additive, The power supplied to the plasma heat source and the temperature of the system determined by the temperature sensing element and the sensing elements located at other strategic points in the system. The power supply to the plasma heat source must be sufficient to compensate for the heat loss in the converter. The process of effectively adding the feed. For example, when the temperature inside the converter is too high, the control system can command 50 200817501 to reduce the power supplied to the 'pulp heat source' (see 窜η二二^^^ See 18, 71-75) Figure), conversely, when the temperature of the melt is too low, the batch 2 ' .· ' system can command to increase the supply of plasma M m M Λ ^ ^ ^ ^ Μ Ά ^ ^ ^ ^ r ^ fi ^ ^ Set The 'should π piece' body ensures that it can maintain the most, t turns: favorable airflow mode) 夂?丨 "Optional supply of one or more thunder will be no ^: Xidian water heat source to ensure the completion: The solid residue in the vaporization process. In a certain apricot, the converter contains a unique vaporization zone (where steam can occur in the absence of electricity) ^ ^ ^ ^ t ^ ^ ^ ^ a Reorganization). ^ · . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . V V V V V V V V V V V V V V V V V V V V V V V V V V V V V V V V V V V V V V V V V V V V V V V V V V V V V V V V V V V V V V V V V V V V V V Or a high-carbon mixture) to the conversion ^ ^ it # T ^ ^ it # ^ ^ # # # ^ # ^ ^ ^ ^ As an additive, the position of the input member can be transferred through the following additives. Ensuring that the feed is placed at a suitable location within the converter to provide optimum exposure to the vaporization heat source. σ In one embodiment, the control system includes a response element for adjustment via the processing element Feed rate, To maintain the product gas in a state suitable for the selected downstream application, for example, the rate at which the feed is fed to the converter can be adjusted to aid in the efficient conversion of the feed to the "appropriate product gas." The rate of addition of the feed is selected according to the design specifications of the vaporization process, and a characteristic value representative of one of the inductive properties of the product gas is maintained at 51 200817501. In an embodiment, control: the system passes through the processing element (eg, wheel Into the component) to the full feed rate 'to ensure that the feed is fed into the converter at an optimal rate, to hold the downstream, arbitrarily dispersed, operating pressure and feed particles, size ^等^ See the 5 components:气动 Pneumatic transmission % system: one piston Tai Shuang rotary valve system or a top gravity feed: system. . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . Form or liquid form. For the vaporization of solid waste, the waste is introduced into the converter via the solid waste feed bee. The converter can also be designed to optionally contain a liquid waste feed port for treating liquid waste. • . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . In the embodiment, (d), in order to improve the efficiency and achieve a suitable product gas, the feed may be pretreated by means of edge grinding, grinding, chopping, etc., to reduce the overall volume or increase the ratio of surface area to volume. In another embodiment, the feed may also be pre-dried in advance to remove any residual moisture. 1 For example, in certain embodiments, a vaporization system suitable for use with the control system of the present invention may additionally Contains a municipal solid waste (ivisW) minced system. The msw mincing system can include an input conveyor, a mincer, and a pick-up conveyor. Control system transfer from remote control 52 200817501 • Stop, start and transfer rates for the belt to meet process requirements. The transformer can be placed in the groove to know the control system when there is no material. The mincer can be equipped with an automatic stop to automatically reverse the blockage and then restart when the blockage is sensed. In a real Qin mode, if I still block, the mincer will be shut down and transmitted - a warning message to the control system. Crushing and disposing of life and tempering disasters: : . " ...· , * .. . . ... lioppeO ’ can be used as an umbrella bridge to feed the converter material = sister buffer

local. The feed cotton can be equipped with an inductor such that the sensed height can be used to control the flow rate of the self-grinding system into the feed tank. The Qin belt can be selectively controlled by the control system so that the waste feed rate can meet the sound making requirements. In some embodiments, the MSW feed conveyor can include another acceptable high carbon content. The entrance to the material (for example, minced plastic), which responds quickly to the process requirements for higher or lower carbon input to meet the gas quality without the need to set a second input on the converter. point. In some embodiments, it is suitable to use the control system of the present invention. The system can also include a plastic processing system to prepare the plastic to a high content. Feed and / or additives. The current urban recycling schemes result in a large number of non-recyclable poem materials that must be sent to the burial. These materials can be used as high-recharge feeds for the vaporization process, and plastics and the like are input to the converter. Before you can break the rhyme. The plastic system can be designed to store the received plastic, smash it, and put it into a pile, which can be fed into the converter under individual control. 1 磙糸 can contain a storage device, a miner with a wheeled barrel, a take-away conveyor belt and a pile of piles 53 200817501 (stockpile) 〇.ll 卜' can be minced using a feed conveyor Dip into the converter. The push-pull ^ 砰 plastic can be equipped with a height detector in the inlet bucket to a low condition. This pass from the h ^ ^ ^ ^ ^ ^ ^ ^ not high and send ▼ action can be controlled by the control system i _ ΐ # ^ ^ ^ ^ fi ^ ^ ^ ^ ^ ^ ^ * in the hair _ add The material loses 'People's blessing: strain. .... . . . . .,.' . Refer to the first 1_4, 仏24' map, can be added to the converter to promote the product oxygen of V carbon body. Carefully select the type and quality of the additive to allow for: the conversion of the feed can be optimized, as well as the gray dimension. Regulatory requirements: 丨, the seat minimizes operating costs. Steam entrainment can be used to promote sufficient free oxygen and hydrogen to maximize the conversion of the input waste decomposition elements into fuel gas and/or non-hazardous compounds. The buckle can be input: gas/oxidant to help the chemical balance during the treatment, to maximize the process of hard turning the fuel gas into a minimum of carbon (the lowest degree of carbon) and maintain the optimum processing temperature while allowing relative High cost plasma heat input is minimized. Carbon-rich additives, which can also be used as an additional and/or supplemental feed, also . . . - * β . Can be added to supplement the carbon content of the feed being vaporized. Establish and control the quality of each additive for the selected downstream application. In certain embodiments, the amount of oxidant injected can be carefully established to ensure maximum return on the relatively high cost plasma arc input heat while ensuring that the overall process does not tend to undesirable process characteristics (related to combustion). At the same time, and meet (or even better) local area emission standards. For the purpose of power generation, it is preferred to manufacture a fuel value having a high value of 54 200817501 (i.e., an ancient force (7) and/or a low heating value, '). The control reaction conditions can be controlled (for example, by adding a twisted t' converter to each of the conversions, a plurality of additive inputs can be included for adding, chaotic, vocal, enthalpy-rich air, vapor: Or a gas such as sputum and iodine continued: 4 ^ ^ A 4 〇, ί ^ # Π-Γ ^ x * # ^ 1 ^ ^ ^ ^ ^ ^ # ^b I, ^ ^ ^ ^ ^ # , b; 〇t ^ ^ ^ ^ 4 € ^ ^ ,;: ^ ^ # ^ ^ ^ ^ ^ f Product gas quality. Can be: policy < origin around the converter or in the converter 4 Qin this air / oxidant front People, in order to increase the treatment area covered by the additive, the additive rounds may also include a sputum for the addition of carbon-rich materials, which may also be via additional and/or Addition to the feed input member of the present invention. The feed useful for the vaporization process of the present invention may be any carbonaceous feed, and the carbon content itself may vary widely. In one embodiment of the invention, The system provides a layer of ice-added carbon-rich material to supplement the carbon content of the feed that is currently being vaporized, as is the special turtle carbon-containing additive. The carbon-rich material may also optionally be added before being mixed with the feed prior to being added to the converter. Providing a feed having a high carbon content increases the carbon balance of the gas produced. In one embodiment The control system includes means for controlling the addition of a carbon-rich feed by utilizing a processing element (eg, a response element) to condition the reactant such that one or more characteristic values of the induced characteristic are maintained 55 200817501 * . - * - . -.··. · . . . . . . . : : : : : : : : : : : : : : : : : : : : : : : ( ( ( ( ( ( ( ( ( ( ( ( ( ( ( ( ( ( ( · ' ': . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . Characteristics of the production of poplar gas). For example, additives can be added to the converter to promote efficient conversion of the feed to the appropriate product gas. The discs and qualities of the foreign objects are consistent with the objectives of the above product gases. In another embodiment of the present invention, the tanning system includes a response element addition to maintain the product gas: in the Li Shi mode, the maintenance is maintained, and the book rate is: the manufacture of the gas. 'Respond in another implementation; to control the addition of three or more additives to maintain the production of appropriate product gas;

: in an embodiment comprising a one-stage process (ie, both the vaporization and the heavy group steps occur in a "single chamber converter"), strategically surrounding the conversion or setting an additive input in the conversion funnel, It may be advantageous to ensure that the additive in the imaginary zone is covered by K vaporization and weight, and the steps are carried out in individual areas of the system. 1 Certain additives are input 埠 (eg 'Vapor Wheels 埠It may be advantageous to set it in the vicinity of the area where the humbleness occurs due to heat hardening. In a more advanced implementation, the control system includes a reciprocating member to base various sensing elements and computing components (straight Use the above = yuan to estimate the composition of the feed) and self-monitoring and spelling, to escape the evidence, to adjust the amount of rotation of the additive β can be ^ ^ ^ ^ ^ ) ^) adjustments such as air, Gan and / Additions such as carbon-rich materials are used to obtain some product gas characterization data. It can also be intermittent. 3 56 200817501 Therefore, the control system of the present invention comprises a suitable downstream application according to the definition of each gas. Pre-product gas poor Monitor the resulting characteristic values to introduce the addendum to the components of the system (as in response to the component >? For example, when the scorpion sensor detects the sand t-stab system will drop: low transfer: to the converter 呐 ^ carbon The amount of production. ..... . . ; ; ; ; · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · , analyzers or other such types of sensors to determine the amount of oxygen in the X-worm flow ^ 丄 丄 丄 疋 疋

Depending on the rate) your oxygen system I wants 0 - carbon monoxide. If the amount of enthalpy in the system is too low, the win will result in a significant amount of TG carbon or carbon black, which will eventually block the equipment downstream of the converter. If there is too much oxygen in the system, it will make the process requirements for the purpose of manufacturing fuel gas... In response to the fact that there are too many flaws in the system, the appropriate signals from the control system can be used to reduce or eliminate the injected Any vapor or air/oxidant (see paragraphs 18, 7 and 7 1 - 5 5). In one embodiment, a synthetic gas fuel value determination module can calculate a low heating value LHV = c1*[H2] + c2nc〇], where cl and c2 are constant and [Η2] and [CO] are analyzed by syngas. The value obtained in the device. The module is operatively coupled to a fuel:air ratio controller, for example, to operatively control a total MSW + HCF feed rate, and or operatively control 57 200817501 MS W/HCF ratio controller and Intercept the sequence controller. In one embodiment, in order to determine the amount of air additive input into the system, to obtain ., ' . . . . . . . . . . . . The composition, or the range is suitable for the energy efficiency and/or consumption of the gas of the dance product, etc., can be danced..................................: The system is set to be A control parameter is calculated based on the characteristic value of the desired LHV (i.e., using [h2] and [CO] for analyzing the synthesis gas:). For example, by setting the temperature and pressure constants or at a desired set point, an overall system parameter can be experimentally defined so that the line input calculation ([LHV] = can be used to correctly evaluate the air input parameters, where a is A specific system setting and , . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . · The amount of gas and steam added to obtain a suitable composition for the downstream: the composition of the synthesis gas composition, or its range is suitable for inducing the energy efficiency of the product gas. ' .. . . . . . . . . rate and / or consumption rate, etc., the control system can be set according to [H2] and [C〇] •......... . . . . , the required value to calculate a control parameter, for example, by setting the ice and pressure constants or at a desired point, experimentally demarcation of the overall system The parameters are such that the formula shown in the following formula can be linearly calculated correctly*. . . . * * . _ Evaluate the air wheeling parameters, — ~ ab Air CO cd A vapor - Μ where a, b, c and d are experimental constants for a particular system setting and desired output characteristics. Those skilled in the art will appreciate that although the invention has been simplified to a linear system of 58 200817501, this embodiment can Extends to other features, so it can also be used to record and calculate other control constants. It can also be used to further accurately calculate control parameters to help limit the more severe downstream applications. In the conversion of the piano, the conversion into fuel is the bite of the ''requires $ for energy to the reactants. In one embodiment of the invention, the vapor part is oxidized by the conversion: Lord 1 to mention: for ^ • . - - . * * - · * The introduction of oxidant into the converter can be partially oxidized in the converter to create partial oxidation conditions, the breaking system in the feed and also complete oxygen The required stoichiometric amount of oxygen is sufficient. Because of the available oxygen, it is very limited, so the solid carbon is converted into carbon monoxide and a small amount of carbon dioxide, thus providing gas in the form of rhodium. The niobium oxidation also releases heat energy, thus Reduce the need The electric heat collecting form is introduced into the energy in the converter. This increased thermal energy can reduce the power required to generate specific reaction conditions in the converter. Therefore, the fuel chlorine is in a power generating device ( That is, most of the electricity generated by conversion into electricity in fuel cell applications, gas engines, etc., can be supplied to a user or to power output 'because the plasma heat source needs to be used in a power generation system using such an oxidant-added system. Get less electricity. The process of converting into fuel gas and help to maintain the best needed. At the same time, the cost of a relatively expensive plasma heat source can be... 59 200817501. Carefully establish the > primary enthalpy of the enthalpy (CO and C 〇 2) that can be removed by gas treatment to achieve maximum β, while the vaporization reaction of carbon (oxygen combustion) is exothermic, therefore Can generate a lot of heat. This will be less reliable than the cost of using two more plasma heat sources, while at the same time helping the wood-related process characteristics associated with combustion. Although when there is a part that is also oxidized, the apricot can be burned in the conversion. ' . . . . . . . . . . . . . . . . . . The feed is oxidized to release energy, so a small amount of alkali gas is available for the power generation device.) The less electricity consumed by the plasma heat source can compensate for the possible loss of sound and electricity. In a real, · . . ' : ... . : , · ' . . . . . · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · '........ " · · · · The value of one or more characteristic values used to maintain the induced characteristics is within a defined range (which is defined as a range of product gases suitable for downstream applications:) At the same time, and the whole .. . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . The additive is selected from the group consisting of air, oxygen, and oxygen-rich air, steam or carbon dioxide. In those embodiments where the dioxon is used as the oxidizing additive, the carbon dioxide can be recovered from the product gas and recycled back to the additive gas stream. In some embodiments, an oxygen feed system is provided to allow process air to be evenly distributed in the region where the two vaporization processes occur. ν In an embodiment, the heated air is introduced via a perforated floor. To avoid clogging the pores during the process, the pore size can be chosen such that it creates a restriction that causes a pressure drop across each orifice that is sufficient to prevent waste particles from entering the pores. The holes may also be inclined outwardly toward the upper surface to prevent particles from being trapped within the holes. Although the multi-stage horizontal design is taken as an example here, but 60 200817501 can include any number of stages, the gas design of each stage can be controlled separately. In the example of this embodiment, in the stage of the sputum, the calcium is as seen by the gentry. In an embodiment, the individual: the floor of the gas can be used to make a far single: the unique emptiness and the averaging of the eight. -. . *. . , ,.'·..· .. : ' -. · " ' Things. For example, if it passes, the standard ^ a ^ ^ ^ ^ ^ ^ ^ ^ ^, a ^ ^ ^ ^ ^ ^ ^ ^ ^ 0 for those gas gas 5 engine from the product gas green matter I composition is higher A ratio of nitrogen to _ in the 'air can be used as an oxidizing additive. However, for the system in which Qin gas is used to generate electricity, the product gas is contracted in use. In such an embodiment, if the product gas age nitrogen will cause an increase in the energy cost associated with the compressed product gas, some of the product gas is not used to generate electricity. Thus, in a particular embodiment, it may be advantageous to use an oxidant containing a low proportion of oxygen, such as oxygen or oxygen-enriched air. In the present invention, it is expected that it will be advantageous to minimize the oxidation of the fuel gas in the converter by using the fuel gas generated by the vaporization process to generate electricity. of. In order to compensate for the reduction in fuel gas production due to partial oxidation, helium vapor can be used as an oxidizing additive. The use of steam as an additive helps to promote sufficient free oxygen and hydrogen to maximize the effect of converting the decomposition elements of the incoming feed into fuel gas and/or harmless compounds. 61 200817501 For the implementation of electricity generation for the purpose of ' ^ ^ ^ ^ ^ a 〇 ^ m ^ ^ ; I ^ . ^ ^ ^ ^ ^ generation - touch ^ human umbilical can understand the introduction of non-r^ synthesis gas. The qi of the traditional skill, the addition of the child's it. (mainly empty ι ~, the gas r state φ and ^" wait until the converter, and the beam ^ gas, the product t hydrogen body琰 琰 可 可 ^ ^ ^ ^ ^ ^ ^ ^ ^ ^ ^ ^ ^ ^ ^ ^ ^ ^ ^ ^ ^ ^ ^ ^ ^ ^ ^ ^ ^ ^ ^ ^ ^ ^ ^ ^ ^ ^ ^ ^ ^ ^ ^ ^ ^ ^ ^ ^ ^ ^ ^ ^ ^ ^ ^ ^ ^ Figure, a carbonaceous feed suitable for use with the control system of the present invention. 2. The A-shake system can also be used to manage the solid residue of the vaporization process from the "dry", for example, solid residue adjustment. 'Used to convert solid by-products or residues produced in the conversion process from feed to to energy into a low-leakage homogenate; the control system of the present invention can control the pill f 11 plasma The rate of heat and the rate of input of the solid residue 'to maximize the conversion of solid residue_to-six to promote complete dissolution and homogenization. V. In the embodiment, the solid residue adjuster contains - Solid residue conditioner for the following components, including: solid residue inlet Plasma heating means to marry every outlet, select

One or more bee ports of the sex setting, and the lower dimension of the W. 汉 汉 汉 汉 汉 汉 汉 汉 汉 汉 汉 汉 汉 汉 汉 汉 汉 汉 汉 汉 汉 汉 汉 汉 汉 汉 汉 汉The control system of the present invention may also be provided with: an inductive element for monitoring temperature and pressure within the solid residue regulator; a response element for effectively regulating the conversion of solid residue into slag, and: controlled by processing means, components For example, power to plasma heat source and solid residue input 62 200817501 rate and other operational parameters. The solid residue conditioner is adapted to treat solid residues from any process that can hinder the feed to different energy forms. This solid residue is typically a device in which the granule form can be from one or more of the gas eliminators. The heat of the probe is heated enough to turn: the solid salt is: the material of the Wenjia # γ is brought to a first point to detract from the deer to make the same body residual body residual Yang adjuster can also help capture: pollution in the slag Solid (hearts like 'heavy metals, and help to form a clean, homogeneous value) slag product. :: ^ ^ • . · ' · : · · · · · · · · · To ensure that solid residues can be effectively treated completely, this solid-state γ residue adjuster can be designed to provide sufficient residence time in solid ▲ H ^ ^ ^ ^ ^ ^ ^ ^ ^ ^ ^ ^ ^ ^ ^ ~ % in the remainder adjuster. In one embodiment, the system provides a tear time of at least 10 minutes. In another embodiment, the solid residue adjuster provides a residence time of up to one hour. In another embodiment, the solid residue s (the regulator provides a residence time of up to 2 hours..., continuous or batch mode) from one or more upstream processes, via appropriate delivery members (known to the skilled artisan) Well known, the solid residue formula can be removed from coke, ash 'melting slag or some combination thereof. In the embodiment, the solid residue is propelled into the solid residue conditioner via a box or transfer screw of the system. Ά For example, you can use the rotating screw or auger mechanism to tie the 63 200817501 threaded edger to transfer or you can use the inter-fire damage to the solid residual adjuster, - ' ; * ' . The residue. In one embodiment, the solid residue input member connected to the solid green K is a system of transfer or load arms. In this embodiment, the shoulder control paper can use the limit switch to control the length of the impact of the load arm so that the amount of material that can be fed into the transfer device per impact can be controlled." The invention control system can further include A control member that can control the input speed of the solid residue in order to ensure that the grafting and averaging of the solid residue are optimal. .. . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . In one embodiment, a heat source is used to heat and melt the ash: The temperature can be periodically or continuously discharged from the solid residue regulator by a temperature of about 1 300X to about 170 fused slag, which is then cooled to form a solid slag material. Such slag can be discarded as buried earth. Alternatively, the molten slag can be poured into a container to form a mold, each or similar building material for use in a roadbed or cement building. It is further broken into agglomerates for conventional use. . . . , . . . . . . Therefore, the solid residue adjuster can include, the slag wheeling member can also be selectively controlled by the control system In one embodiment. Gossip, the molten fuse holder is discharged from the solid residue trap. The output member may include a slag outlet crucible, which is typically located at or near the bottom of the converter, and a φ φ assisted melt The slag naturally flows out of the converter. There are many ways to control, w仏w slag outflow solid residue adjustment For example, in the embodiment of the animal husbandry, the difference between the temperature of the nearest electric medicine heating member and the exiting space 64 200817501 can be adjusted to control the residence time of the molten slag, that is, by Adjusting the solid ^ a # # M % ^ ^ ^ ^ # ^ # ^ g ^ ^ β can be changed by keeping the solid residue adjuster sealed to change the slag output member to adapt to the minimum heating standard. In the Shih-hsi mode, the wheel-out member includes - a pouring spout or an S-shaped trap. '' . . . . * · . , , , , , , , , , , , , , , , , , , , , , , , , , It may be advantageous to move towards the slag wood %L Α 卢 出口 exit, thereby sighing the temperature to ensure that the mouth of the sputum is open throughout the fog. This way also helps to maintain the melt as much as possible It is uniform. By X, it is avoided that the incompletely treated material inadvertently leaves the solid residue adjuster during the melt extraction process, and the slag can be extracted from the solid residue adjuster in the evening. Μ 从, "月间...了'Extracted by batch dumping: slag or slag During the treatment period R3, I, /, continuous extraction of slag from the continuous '", 1 乂 continuous method. Can be * UJ, ^ # ^ ^ ^ ^ ^ ώ ^ ^ ^ ^ ^ ^ is used to remove the small The sand in the car is thrown into the model: - The wall of the special-purpose, solid residue adjuster is lined with refractory material, which can be used for special high temperature (ie, eight 130〇c^ i80 〇ec).# A kind of refractory material 妯 勺 虹 虹 虹 。 。 。 。 。 。 。 。 。 。 。 。 。 这类 这类 这类 这类 这类 这类 这类 这类 这类 这类 这类 这类 这类 这类 这类 这类 这类 这类 这类 这类 这类 这类 这类 这类A high alumina refractory material that is deuterated with chromium. Solidity can be determined by a variety of factors. The physical design of the θ; π ^ α 凋 整 整 可 可 克 克 克 克 克 克 克 克 克 克 克 克 克 克 克 克 克 克 克 克 克 克 克 克 克 克 克 克 克 克 克 克 克 克 克 克 克 克 克 克 克 克 克It can be brought to 17 to ', melt and temperate temperature, the plasma heating member used, and the position and orientation of the plasma heating structure. V ^ *· · . . : . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . The slag is light. It is used to: monitor the temperature of the adjuster to adjust the thief; ^ wall, or the top, center and bottom of the adjuster's dog material. Mu invention system can also be set to handle the decoration, To control the input speed of the power and solid residue of the plasma heat source: rate, I: . . :: ... , . . . . For example, 'When the melting temperature is too high, the control system can command to reduce the heat source. Power level: Conversely, if the melting temperature is too high, the control system can command to increase the power level of the plasma heat source. The solid residue regulator can be controlled by an indirect control system or through module control. '.· ^ ...... This control system contains a number of subsystems for control. ^ * ' * · ' In one embodiment, the solid residue adjuster may also include components for recovering heat , that is, the plasma heat source cooling member and the melting member in FIGS. 24 and 25, which can be used to check the cooling member. The amount of waste heat generated is small. Such means for recovering heat may include, for example, a heat exchanger. In such an embodiment, the control system may further control the operating conditions of the heat exchanger. There may be multiple temperature sensors, flow control elements, and other such monitoring and response components. 66 200817501 In the embodiment t, the solid residue is withdrawn from the main converter, and the " is fed into a high temperature melting chamber The chamber, after being cooled in the slab, is transferred to the pile ready to be removed from it. In the other, a solid residue feed system is provided, which can utilize the rod The type of transmission «I catches the final solid, and the residue is brought into the melting chamber. This can also satisfy other solid residues. The residue adjuster is in standby _ first sent to another place and then re- Introduced to the fixed-plate residue adjuster feed system t ° In one embodiment, the solid residue received by the residual system is transferred to a small room that is melted and rejected by the plasma. Medium _ dissolve height ◎ And the hand is dropped into a quenching bucket. Eight...-. .- .. ...... ' can be adjusted in the same way as the gas generated by the converter to handle the residue Produced by the device: raw gas (that is, used for the same or different downstream applications). Metals that have not been removed in the MSW treatment system stage can be transmitted ^ ^ ^ ^ r. t ^ ^ ^ ^ ^ ^ ^ f ^ ^ ^ ^ ^ τ Melting, therefore, this small room may be blocked by metal because the metal density is generally high (four). To solve this problem, the temperature of this chamber can be raised periodically to metal (4) and (d) Metal can be removed from the bottom of the chamber room. Because the temperature used to melt the solid residue is quite high, especially for melting the metal therein, it is quite demanding on fire materials. This includes rot 67 200817501 money, especially in addition to high temperatures, including corrosion resistance at the slag level. It# a ^ 0;^ # ^ Refractory material, the rod has better insulation. In some embodiments, the residue can be lifted from the converter and the gas regulator to the solid residue regulator, and the i residue can be combined to make it a solid product. And a syngas that can be adjusted: installed in the converter to form a gas group for further adjustment, crediting and downstream: application. When controlling the solid residue I, you can adjust the plasma torch as needed. The slag chamber ▼ includes various temperature sensing elements and components. In some embodiments, the gas flow rate that can be moved by the downstream vacuum generator (i.e., the syngas blower) can be set at the gas outlet line. Adjust the feed rate of the solid residue regulator as needed to ensure that acceptable temperature control is still at the rate of the melt rate of the torch and to prevent high amounts of unmelted material in the slag chamber... Exchanger. _ ... * * · .... - • , . Refer to Figures 1-4 and 24-26, suitable for use with the control system of the present invention: the s slave feed vaporization system can also be set The heat energy component can be recovered from the scaled product gas via a heat exchanger. The heat exchanger may comprise a 'slip gas-to-air heat exchanger, whereby the hot product gas' may be used to provide the heat energy recovered by the air 1 that has been superheated (to the already overheated:: two gas) The form exists) can be selectively used to provide heat to the gasification process using 'as shown in Figure 26, whereby the reduction must be made by the one or more. A heat source is provided to provide thermal energy to drive the vaporization process. You can also use this back 68 200817501 ‘ . . . . . . . . . . . . . . . . : : The heat collected in any industry or livelihood application. In one embodiment, the temperature of the gas is reduced from about 1000 ° C to about 7401, the same as . . . . . . . . . . . . . . . Increase the air temperature from the circumferential temperature to approximately 60 〇υ. • . . '., ', . . . In another embodiment, this gas-to-air heat exchanger is used, .'.. .. . . . . * * . . . - * ' * to heat an oxidant, such as oxygen or oxygen-enriched air, which can be followed by .. . . . " . 'Guang:...::... and then selectively used to provide The heat is used in the vaporization system. : • . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . .. r . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . · . . · ' · . *. Shape or tube: heat exchanger, both Zheng: is a straight, single pass design, and .. .....: ... · · · · · ·' . . CU-type tube multiple pass design, and flat plate heat exchanger. In an embodiment.......::: ... . . . . . . . . , where the product gas flow in the tube: and the process air flow in the gas-to-air heat. · : · - . · · ' . . . . ... * - , Reverse flow inside the shell of the exchanger. The design of the heat exchanger can also incorporate components such as tubes, tubes, and the like to prevent the tubes from rupturing. How to Choose the Right Heat. The exchanger is the knowledge that is known to those skilled in the art. .., . . . , . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . The system can be further packaged. · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · . Associated separate temperature sensing components. These temperature sensing elements are set. ... . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . .... ... the temperature rise caused by burning. This type of temperature rise is detected and can be used to automatically turn off the induced air blower (which moves the refrigerant air through . . . . . . . ;; : heat recovery system). A lower temperature limit can also be used as an indicator of the start of the pipeline, which in some embodiments can be used to indicate that the system should be shut down - 'for maintenance. This heat exchanger can be controlled by the control system of the present invention and/or a modular control subsystem. Alternatively, the heat exchanger may additionally comprise one or more steam generator heat 69 200817501 exchanger for generating steam which may be used as one of the vaporization reactions. ' . . . . . . . · . . . Addition, as shown in Figure 26, is used to drive a steam engine or to drive a rotation. ... : : Steam equipment, such as an induced blower. The heat from the product gas utilizes a - - ' . . . * * heat exchange member to heat the water to produce a vapor, and the heat exchange members may be • · ..... . . . . . . . . . . . Steaming heat exchangers (eg, Figures 2, 3 and 2.5), waste heat boilers (eg, • . . . . . , . .. Figure 26) and so on. In one embodiment, the heat generated from the shy gas is used. . . . . . . . . . . . . . . . . . . . . . . . . Superheated steam. Referring to Figure 26, there is shown a relationship between a gas-to-air heat exchanger and a steam generator heat exchanger in accordance with an embodiment of the present invention. '-.' .... : .. ... . . . . . , . . . . . . . . . . . This exchange steam can also be used as a steam additive during the vaporization process. · · · · ... ... - - . . . Help to ensure that there is sufficient free oxygen and hydrogen to convert the feed into a synthesis gas • ..... - . . ' . . . . . . . The effect of the product is maximized. Vapors not used in the conversion process or vapours not used to drive rotary processing equipment may be used for other commercial purposes, such as by using a steam engine.. . . . . . . . . . or in local use to generate electricity or It is supplied to local industry customers for -·-·... *-: . . . ... its use, or it can be used to improve the effect of extracting oil from coke. The optional steam generator heat exchanger is referred to in Figure 2, in an embodiment, with an additional heat exchanger (which is controlled by the control system of the present invention) The steam obtained by the output of the steam turbine is cooled after being fed by a cooling tower pump or the like, and the steam turbine is operated by a vapor generated by a steam generator heat exchanger for cooling the synthesis gas. A steam engine, a steam engine that operates with a vapor produced by a steam generator heat exchanger for cooling a gas turbine/engine and exchanging the generated gas, or a combination thereof. In a 70 200817501 - . * · . - . · ... in the implementation of the method of 'departing from gambling, crying, a _ ^ ..., changing time, cooling the gas / water is pumped out And feed the appropriate chemical from a source of soft water to remove the air and excess oxygen, and then send it back to the child's steam generator heat exchanger, the steam generator heat: exchanger, etc. The steel furnace is fed into the water. In a certain two mode, the control system of the present invention can be used to maximize the transmission of energy in the system, and it is difficult to optimize the amount of conversion of the feed-to-energy by the law. Because the heat induced by the recovery to the vaporization system can be reduced: less energy that must be input from the external energy source when drying and volatilizing the feed step. The recovered p is reduced to underweight. Accordingly, the present invention allows efficient vaporization of a carbonaceous feedstock in which the heat source is supplied by heated air (heated by the induction heat recovered from the product gas). In order to achieve the best, the components used to control the heat exchange considerations are changed. This control component is used

The sound disk/gauge, number includes (but is not limited to) the temperature and gas flow rate at a specific position of the system, and the operating condition is adjusted according to the return parameter of the A% surname, so as to maintain the system in the predetermined range. The system can be controlled by the mouth library: "The plant and the body section are included in the air flow rate, the product gas machine catch, the speed of the input feed, and the addition of the mine (such as steam) The speed of the early and the power level of the plasma heat source. For example, a sensor such as , for example, 洚 洚 于 can be placed in a vaporization system with a plurality of specific bits 3 within (and other such sensing elements). These temperature transmitters are used to measure the temperature of the product gas at the inlet and outlet of the gas at the time of the gas, and the temperature of the product gas at the inlet and outlet of the steam generator heat exchanger. . The temperature wheel can also be used to measure the temperature of the process air heated in the gas-to-air heat exchanger and to measure the temperature of the vapor leaving the steam generating heat exchanger. . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . .

: The temperature of the converter will not exceed the load: ideal. I. . , . . : ::, · . ' . . . :· ' .... - . . . . The design temperature of the vegetable gas-to-air heat exchanger is "〇5 0 ΐ:, can be ... · .... * · . . · *' ... , · . . , - . . . The temperature transmitter in the gas vapor of the exchanger controls both the exchange air standby speed and the electrical installation thermal power through the system to maintain the best... · · · '. ' ... .. .. . The temperature of the synthesis gas. In addition, measuring the temperature of the product gas leaving may have ..... - ............. Helping you to recover the optimum amount of product gas from the two heat recovery stages · · · ·. should be hot ...· .... . . . _ In an embodiment, a temperature sensor such as a temperature transmitter. ... ' . . . . can be installed in the air outlet flow To measure the temperature of the heated air, which helps to ensure that the process has been implemented under conditions that ensure that process air is heated to the appropriate temperature available for the vaporization process. In one embodiment, the air outlet temperature of the exchange is about 600 ° C, so a temperature transmitter installed at the air outlet flow can be used to control the system. Either or both of the internal air flow rate and the electric heat collecting power in the plasma recombination chamber are used to maintain the optimum synthesis gas input temperature, which in turn can be used to control the temperature of the heat exchange air. In accordance with an embodiment of the present invention, the control strategy sets a fixed point of optimum heat exchange air output temperature, e.g., about 600 ° C, and the exit temperature of the steam generator heat exchanger, for example, about 235 ° C. Therefore, according to this embodiment of 72 200817501, when the synthesis gas flow is reduced, the gas from the gas-to-air heat exchange .... . . : . V. * The temperature of the gas leaving the device becomes relatively cold, resulting in steam output. Drop, because the exit temperature of the steam generator heat exchanger is also set to a fixed range. :下.V. *. - - - · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · The situation when the air flow is reduced... According to an embodiment of the present invention, the temperature leaving the exchange air is kept constant. The gas that is trapped by the gas-to-river heat exchanger; the temperature becomes ΜM im iL· ^ A i ^ ^ ^ A ^ ^ II II % ^ ^ ^ > f & . · : . . . . . . . . . . . . . . . . . . . . However, as the air flow through the system decreases, the product gas flow will also follow. . . . --: ..... .,: ... . *-. .. · - - Reduces the temperature of the heat exchanger entering the steam generator only for a short time. . . . . . . Sexually elevated. For example, if the air flow is reduced to 50%, the gas temperature at the inlet of the steam generator heat exchanger 50 will be briefly considered to be about 800. ..... * 1C, which is designed for the heat exchanger Within the temperature limit. - In addition, in some embodiments, the control system of the present invention provides a response element for controlling the automatic valve so that when the amount of air exceeds the process demand Pump process air out to the environment. For example, in some implementations, (in the case, because of device considerations (for example, when starting a shutdown procedure), it is necessary to heat a larger amount of air required by the tb process. In this case, It is necessary to withdraw excess exchange air. Referring to Figures 24 and 25, the above-mentioned heat exchanger can also be used to cool the product gas for subsequent specific filtration and gas adjustment steps, mainly with regard to the converter gas regulator (eg , a converter gas regulator cooling member), and a member for providing a cooling plasma heat source (eg, a plasma cooling member), a slag treatment (ie, a slag cooling member), etc. 1 73 200817501 Conversion gas seasoning device reference Figures 1 and 4, the b-month control system is suitable for the first vaporization system. . . . ' . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . Gas adjustment • · ..... ..... ... . . . . . . . . . . , or other gas conditioning components to convert the products of the vaporization process into specific specifications Output gas. Let the product gas pass through the φ ^ adjuster It helps to ensure that the product gas is almost free of chemicals or particles, and that it is dyed. . . . . . . . . . . . . . . It can be used in a soldier-energy production system or in an embodiment to direct the product gas to the conversion 篆*._.***.. ': The gas is here: a specific sequence of treatment The steps are used to generate different ... · · · · · · There are output gases for downstream application specifications. The converter gas regulator contains a plurality of ... .. . Components, which may be implemented may include the following (but not limited to) processing steps; shifting;; . . . = '' · . . . . . . . Substance, acid gas (strict or heavy metal, or the humidity and temperature of the gas as it passes through the system. The sequence of processing steps required is determined by the composition of the synthesis gas and the specific composition of the output gas available for downstream • application. σ can also be used to use this fascination... · ..... ' Control system to achieve the goal of maximizing the converter gas regulator. In one embodiment, a vaporization system In the vacuum extraction condition of the shoulder, the continuous self-steaming system extracts the hot product gas through an exit gas outlet of the vaporization system. A gas transfer member, for example, is used to transfer gas from the converter to the converter gas regulator or Other conduits. A gas/transport member that uses a gas pipe or other similar passage to transfer gas from the converter to the converter gas regulator. One or more converter gas regulators can also be used, such as a primary converter. Gas regulator and primary converter gas adjustment II. Under this control 74 200817501, the secondary converter gas regulator can be used to process materials removed from the gas stream of the main converter gas regulator, such as particulate materials and heavy metal materials. The gas from the gas regulator can be stored in the gas storage bucket (see Figure 3). The feed is fed through the further processing component Shab 4; the processing system is blown, and the feed is fed downstream. In the delivery device: (eg: '第:'"2--图》.:::/. ........ · ' _ to account for the discussion of the 5 but the hot product of the greedy round This ^, Minwei component is helpful. In one embodiment, the heat exchanger is used to perform the ** - . . . - - . . . . . . - cooling step 'by allowing the heat recovered from the product gas Can also be selected: · · 1 ... . . . . . . . . . . . . . . Recycling ^ cycle for vaporization process A (see the first, 4 and 26 Fig.) In another embodiment, the heat from the vaporization system is first utilized as a means of evaporating water in a steaming apparatus, such as the first and fourth reactors. Plus * . . . . ' . to cool. In one embodiment, an evaporative cooling tower (see Section 4., ''..--) can be used to cool the synthesis of the converter gas regulator from the vaporization system. * - - . . . Fluorine. Evaporation The cooling tower can cool the temperature of the syngas from about 7401 to a temperature of about 150 ° C to about 200 ec. This step can be carried out by means of thermal insulation saturation, which involves injecting water directly into the control mode. Steam flow. * . . * . . . This evaporative cooling step is a dry treatment, and can be controlled and controlled by the present invention to ensure that the cooling gas is not humid, that is, the cooling gas is at the cooling temperature. The lower relative humidity is still below 100%. As mentioned above, the converter gas regulator may comprise means for removing particulate matter from the cooling gas and gaseous contaminants that are incompatible with the downstream use of the product gas. Into a particle removal system to remove particles that may be trapped in 75 200817501 . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . In addition to system S4, and Including, for example, high temperature ceramic filter, cyclone separator (see section 7 meat, 〆#, 曰 曰 7 、, T / map), venturi tube brush (see Figure 7: figure), electric pain Gas and light inspection filter (Q particle filtration: water brushing: ethnic, or fiber, etc.:, all of them are gas-fired ^^ 1 type shell 4 rabbit 0 different sorts of various types of fluorine cleaning steps for more efficient use He kind of r; body cleaning device. W〇/2〇〇6/1282 8 5 and • . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . * * . ' . . . . . . . . . . . . . . . . . . . . . . . . . . . Provides a removable product gas: the structure of mercury or other heavy metals in the body.: .'· . . . For example, a dry injection system uses a calculated amount of activated carbon, .....*; . . . . . . . . . * * * * _ . It is injected into the air stream and stays in sufficient time. The heavy metal adsorbed on the surface of the activated carbon on the surface of the activated carbon that can be adsorbed by the heavy metal particles can be captured by the fiber bag filter or the wet ESP system. In one embodiment, the converter gas regulator may alternatively comprise a . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . In this case, the system may need to pass 4 heavy metal gases through a packed tube filled with a low pH (generally (1-2) circulating solution. Dry scrubbing or wet scrubbing can be used to reach acid gases. Removed item's. Dry wash The main part is a spray type dry adsorber and injection of baking soda ash or lime powder before using the fiber filter bag filter. In one embodiment, an activated carbon mercury polisher is used as a component for removing mercury. (See Figure 4.) An activated carbon filter bed can be used as the final polishing unit for heavy metals. 76 200817501 An acid recovery subsystem can be selectively connected to the converter gas regulator. . . . - *'· · Whole unit' to recover sulfur or tannic acid and hydrochloric acid (from the carbonaceous feed) with commercial debt. The acid removal system may include a scrubbing system (ie /, HC1 scrubber), acid . . . . . ....................................................................................................................................................................................................................................................................................................................................................... The function of the humidity control member to control the element is to ensure that the fishing degree of the output gas is suitable for the lower part of the article. *........-.. " . . . For example, the humidity control member may include To cool the airflow so that * - : *; · · · . . , , · . . . . . . . . . . . . . . . The condensed water can be removed by • · _ . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . In one embodiment, the gas treatment system may include an elastomer for the recovery of the oxidized and/or ammonia and/or chlorine and/or sulfur elements - suitable components. ' . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . In an embodiment, the control system can sense that the process efficiency of the converter gas regulator is degraded or insufficient, and the airflow is transferred to A backup* . . . . . . . . . process or injury tamper system V. In another embodiment, the control system can provide means for fine-tuning the steps of the converter gas damper, And make . . . . . . . . . . . . . The control system of the present invention may comprise an inductive element for analyzing the chemical composition of the gas stream through the converter gas body regulator, the gas flow and thermal parameters of the process, and a response element for adjusting the gas regulator within the converter The condition optimizes the processing and composition of the output gas. " Constantly adjusting the reactants in this way (eg, injecting activated carbon with sufficient residence time, controlling the pH of the HC1 scrubber), so that the process can be optimized according to the designed specifications and 77 200817501. Homogenization system 1: .... .. . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . The chemical composition of the product gas at least partially homogenizes and adjusts the properties of the gas such as gas, pressure and temperature to meet downstream specifications. · : : J Axe artisans can understand that this vaporization process is a change in the temperature, flow rate or flow rate of the factory.

C

(Moving the raft selectively provides a capture member shape or presence, which can be used to deliver: a lower variability of gas for downstream applications. ^ Provided in the implementation of the ten invention a homogeneous system that collects gaseous products in the vaporized image and reduces the gas in the homogeneous system^

The variation 1± can also optionally be used to help adjust the characteristics of the gas such as flow, pressure and temperature with other components of the system. V. The homogenization system provides a gas homogenization system (see 1st 4 of Implementation Force 1). 6 〇, 6 7 and 6 8) or dimensions designed to tolerate one help. * A similar system for achieving a relatively uniform gas stagnation time. The other components of the homogenization system can be designed to help achieve downstream application specifications, as described above. This control system can be used to actively control the various properties of the product gas before it enters the squalor system, so that once the gas is output from the homogenization system, its characteristic value That is, the downstream application specifications have been met. The composition of the product gas entering the homogenization system is determined in the vaporization process. The adjustment of the control system in the vaporization process allows the product gas to be optimized to specifications for specific downstream applications (eg, gas turbines or fuel cells used to generate electricity, etc.). Therefore, it can be used for a specific capacity technology (eg, for specific gases, 2008, 2008, or for the thirsty wheel), and for the best overall conversion efficiency, depending on the type of feed and additives used. Adjust the operation of the vaporization process to customize the product gas composition. The production and materials of the detachment vaporization system are surrounded by the changes in the product itself (eg, changes in feed composition and rate, and changes in air brigade and temperature). . v .... . . . . . . . . . . . . ^ ^ ^ ^ ^ Inductive elements are used to monitor the flow rate and temperature of the product gas to maintain the fluorine parameters within a predetermined range suitable for the end use. The adjustments made by the control system must take into account the residence time in the homogenization system to ensure that the product gas is suitable for downstream application specifications. This homogenization system helps to reduce the product gas flow rate and: : · · · · · · · · - Temperature Changes in the residual. For flow rates, these changes occur in seconds. · : · * · · * . As for temperature changes in minutes. The homogenizing system comprises one or more gas homogenizing chambers, or the like, having a product gas inlet member, a homogeneous gas outlet member, and optionally an emergency outlet port. The homogeneous system absorbs gaseous products produced from the vaporization system and promotes product gas mixing to reduce variations in the chemical composition of the differential gases within the homogeneous system. Other variations in other gas characteristics, such as pressure, temperature, and flow rate, can also be reduced during mixing of the product gas. The size of the homogeneous system can be designed according to the execution characteristics of the upstream A-chemical system and the requirements of the downstream mechanism, so that it can meet the purpose of the minimum chamber. This homogenization system is designed to receive the product gas from a vaporization process and to protect the residue. The retention time is the product gas: the body is sent The time before the downstream equipment is in a homogeneous system. Lean Yao Yi I m e sa j time:. The retention time can be chosen to be proportional to the response time associated with the vaporization system controlled by the control system of the present invention. 修正 Correct the remaining of the vaporization (four) changes _ fall in the purpose of the pre-finishment _ The amount must be long enough to determine The value of the hospitality is: _ within the application's booking range and control: System: Whether to adjust the nine to correct these changes. In addition, the time during which the product gas stays in the homogeneous system can also be obtained from the product a μ # ^^ ^ t ^ ^ ^ ^ ^ ^ φ . ^ t ^ t ^ ^ $ μ a ><# iE ^ ^ t ^ ^ ^ ^ The shorter the time. • * . The control system of this specification can be used to control the vaporization process so that when the tool uses a homogeneous system with a specific residence time, the product gas will meet the stability characteristics of downstream specifications. In general, machine builders will provide specifications and tolerances for specific machinery, which are well known to those skilled in the art. The following description will be made with reference to the embodiments. It is to be understood that the present invention is not intended to limit the scope of the invention. Embodiment 1 In this embodiment, please refer to Figures 27-72, which provides the invention of this invention 2008. - - ' ' Details of the embodiment and various options. This embodiment presents each subsystem of a vaporization system suitable for use with the control system of the present invention and demonstrates how it functions to be used to municipal solid waste (MS W ). Converted into electrical energy..... . . ....... : : Part of the integrated system. The subsystems discussed in this example are: a poor ^ ... ' - . - - - · · · · · · · · ··························································· Plastic processing system ^ Horizontal semi-transfer unit of the horizontal direction vaporizer, gas weight ^ :: Full ring system:, a good gas · · · · · · · · · · · · · · · · · · · · · · · · · ················································· Together with a control system of the present invention, a functional block diagram of the entire vaporization system 120 of the crucible, the vaporization system 丨2〇. is mainly set to -. . . . Gas, and has the relevant reorganization, adjustment and homogenization of the synthesis gas in the gas engine 9260 to attack power generation. Pi City solid waste fMSW) care system cake / ... .. .: . The design of the original MSW processing system 92〇0 included the following: (a) 4 days of storage capacity; (b) avoiding long-term over-disassembly; (c) preventing debris from being blown everywhere; ) control the smell of 〆 (uniform waste (garbage unloading available in and out space; (f) loading 9218 The minimum shipping distance and delivery time required to transport the MSW to the MSW mincing system mo from the reactor 92〇2; Cg) avoid interference with the loader 9218 and the garbage truck; (h) allow factory expansion The possibility of additional vaporization flow; (1) The lowest intervention caused by the truck entering the equipment, especially in the danger zone: (1) the safe operation of the least personnel; (9) to tell the loader to operate the filling height of the input hopper 9242 in the shell conveyor Instructions; (1) smash the received waste into pellets suitable for processing, and (m) remote control into the 81W1717501 into the processor MSW idle and independently control the plastic feed rate (to be detailed in T )- • .... . . . . . . . . . • MSW: The processing system 9200 includes an MSW storage building 9210, a..-:--. . . . . · ' ' ' _ . · · · · . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . System 9250 is used to store, smash, pile: sound and feed high sound materials (in this case a non-recyclable factory '..' · · · ' . . Glue), its feed rate is used as this vaporization

Figure 30 shows the overall layout of this sound system location. All MsW: ...' ..... . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . ... ' ' . . . . - . · - . . . 'The flight of the 糸 糸 1 1 1 1 1 1 ' ' ' ' ' ' ' 以便 以便 以便 以便 以便 以便 以便 以便 以便 以便 以便 以便 以便 以便 以便 以便... • · · ' ;. ,··.. ·' · · · . . . . . . A first-in-first-out (FIFO) scheduling method to make MSW Excessive decomposition is minimized. This FIFO scheduling method can be implemented by storing trucks and loaders in the sector. The MSW is removed from the end of the building while the material is being transported by the loader 9218 at the other end of the building 921〇, thus allowing the loader 9218 to operate quietly without interference from the truck. When the loader 9218 has moved the material back to the approximate center of the MSW pile 9202, that is, when the "old" material has all been used, the loader 9218 will be swapped to the other end of the Msw storage building 9210. Continue. In order to minimize the volume of the MSW storage building 921, the working truck is tied outside the MSW storage building 9210. This also minimizes the size of the door 9212 because it only requires the truck to be poured straight in, as well as the ability to control debris and odors. At any time of the day, just open a door at b 82 200817501, so that the door mu only needs to open for about an hour every day. — "· ... , ·—— . : * The nth picture is the layout of the MS W staggered building 9210. The MS W storage structure 9 2 1 0 has a wheel conveyor π22' for separating the M SW pile 9 2 2 2 and the channel 9 2 1 6 code wall 9214 MSW itch system wo. · · · · · · _· * . , - ; , · -'. . . - _., . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . - Can go from the MSW pile 9:2〇2 to the storage, and the 921 〇 does not need ..... :* ' . ' . . : V: ·- · ·· ' . . MS W★ Deposit 9210. Therefore, the door 921々 of $ ..... ·- can always be closed, and the other end team is opened when it is unloaded. • . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . The truck can be stored in the MSW storage building 921 〇 both ends. ···..·. '* · -, . . . As shown in Figure 28, it can reduce the space and truck movement in the medium... .... * Range of motion · Requirements for both. This spatial layout allows the truck to be driven into the equipment, poured into the MSW storage building, “removed, removed and returned directly to the road 9204, at any time, without approaching any process equipment or Operators. These two ways of guiding the entrance can also avoid the need to have a road in the equipment to allow the truck to enter and exit the MSW storage building 9 at both ends of the 10th. A mechanized, barrel loader 9218 is used to transfer material from the pile to the mincing system. A slip loader design is used because of its small size, ease of handling, etc. Standard commercial skid steers have sufficient capacity to feed MS W Clean the pile floor after unloading the truck, and handle the waste plastic system mincer and process the feed. 83 200817501 This MSW mincing system is made up of —·: a pick-up belt and a magnetic pick-up book wheel into the pass. , a mincer, MSW storage structure is divided into 2 ~ into. This wheeled conveyor 9222 can be taken from the inside of the machine. This feeder's feed hopper, special transport Msw and drop it into the feed hopper can hold material about f ° This conveyor has a deep groove, Add: Object 9210: External concave ridge ^ : : The feeder is controlled by the process controller to make it so that it meets the process requirements. The translator can read the amount of MSW in the hopper from each case. The high Z machine breaks through any bag and breaks up the large pieces of material into small pieces suitable for processing. It can guarantee that the MSW received is suitable for the process. Because the selected VISW can be included in the body. Or for the smashing machine: the extremely hard item causes the mincer to get stuck. Therefore, the mincer must also be equipped with a blocked hair... ··....· . . . . . . The device that automatically stops when it is born automatically turns to clear the obstruction and restarts. If the debt is blocked, the grinder closes and sends a warning message to the controller. The shredded waste falls into a belt The conveyor is transported under the control of a magnetic pick-up system and then falls into the hopper of a screw conveyor, which feeds the waste into the carburetor 2200. To avoid inadvertent feeding of excess iron-containing material In the carburetor 2200, a magnetic pick-up device is disposed above the pick-up conveyor to smash the waste The magnetic material is sucked in. There is no non-magnetic 84 in the opposite direction of the pick-up conveyor. The 200817501 messenger 'between the magnet and the scrap, so that the ferrous metal attracted by the magnet can be horizontally discharged from the scrap pile f Remove. After that, remove the iron-containing metal from the magnet and drop it onto the waste pile to be discarded. 丄This: MSW feed system is from the hopper> ^ Transfer the waste from the ash system to the waste , ^. Mo paid to the heart of the I-amine room 22〇2 in the β-smashed waste

^ it # 4^ ^ ^ ^ ^ S Material: - Slow _. ^ ^ ^ ^ ^ ^ ^ ^ ^ ^ # 4 t „ ^ ^ ; it ^ , # ^ ^ # ^ ^ The controller is controlled so that the waste feed can meet the demand of the process. ## # it II ^ ^ ^ % ^ 4 ^ τ ^ 4 ^^ ^ ^ ^ Fruit. This input is attached to the mincing system and has a lid to control debris and odour. This MSW feed conveyor also has another _ inlet for Bite μμά^α^_ -' . -.· · .: '.·'.' ; , ' . . . . . . . . . . This vaporization system ΐ 2α provides additional plastic as a process addition 2 plastic It is separated from the MSW and sent separately: into the vaporizer ^In #. The system used to process the plastic is designed to provide a plastic storage place for the J, and then it is ground and placed in the material. And is sent to the processor under independent control. The system consists of storage equipment, a miner with a feed hopper, a splitter, and a pile, all in one common structure to control the crush The sputum feed conveyor moves the minced plastic into the processor. The plastic storage building has the capacity to store two trucks of plastic bales, one side of which has only one opening on one side. The building can also protect the mincing system and control the swarf and protect the minced material. ^ ^ t#^ ^ ^# # ^ ^ In the pile. 匕乂_ : : 'Set the input hopper of Dan 怦 ^ Because of the value, off w * : because, Yunyi is outdoors ^ ^

The roof and the law are off. Seal the groove of this transmitter [gel, ^ open to the vaporizer 22 〇〇 opportunity. The screw conveyor here has a gas-tight effect when it contains material. The detector in the hopper displays the high and low water levels and has a mirror for the sliding driver to monitor the filling height. The action of this transmitter is under the control of the processing controller. Converter 1200 - Converter 1200 comprises a vaporizer 2200 p and a gas recombination system (Gas · ··· . . . . . - - ' Reformulating System, GRS) 3200 〇MSW and plastic are fed into the carburetor 2200, and The formed gas is sent to the GRS 3200 where it is recombined. Any residue from the carburetor 22 is sent to a retentate adjustment system 4200. The carburetor 2200 is designed to take into account the following requirements: (a) providing a sealed, insulated space for the primary treatment of the waste; (b) Introducing hot air and steam through the vaporizer 2200 in a controlled and dispersed manner; (c) enabling the height and movement of the waste pile passing through the vaporization 86 200817501; '. ...., the apparatus 2200 to be controlled; (4) providing control The instrument of the vaporization process; (e) delivering the gas to the GRS 3200; (f) the second shifting residue for further processing; and (g) providing the internal access for the detection and maintenance. ..... . . . . . , . . . . . . . . . . See the pictures of Figures 32 to 35: The first steam-filled chamber MM It has a feed inlet Μ. 4, with the addition of * ·.* · . * ·. . . * - -:, . . ..., eight to the hot air inlet, 舆GRS direct far: pick: it is also in the center. The residue of t is + mouth. 2 2 〇 8 to . and .. various. Maintenance. 2 22 0 and. In. out. 2 2 2 2. 埠. The vaporization chamber 2202 is constructed as a steel turn#: a step grade 2222, 2214 V such as 223 0 v 2232 ^ ^ ^ ^ ^^ # ^ # ^ ^ # ^ ^ ^ ^ ^ 22〇〇» ^ ^ ^ ^ ^ r ^ . Pressure sensor and inspection 埠. . . . , , . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . Damage, and also minimize heat from the system: solid ^ " unnecessary loss of the crack. See Fig. 36 for a multi-layer design of the refractory material. Right-handed: There is a chromic oxide layer 2402 on the inside, a high-density alumina layer in the middle, and a very low-density insulating sheet 2406 on the outside. The refractory material is used as the inner lining of the metal casing 2408 which is divided into V. The vaporization chamber 2402 is further lined with a lotus rot (4). The step-by-step protection is not affected by the steps of the vaporization chamber 2402 - I* white 2212, 2214, 2216 each have a perforated floor 2270 through which the enthalpy is 丄>* thermal emulsion. The size of the air hole is chosen to limit it, so the pressure drop across each π-t hole is sufficient to avoid waste. 87 200817501

This p is the temperature of the ladder [good ^, 9003⁄4 V: the bottom of the skin range. Dijon | Temperature range between 1000 art. Referring to the third step 22丨2, 2! 4 and 2216 of the step floor, the vaporization chamber 2202 is divided into three processing stages, and the pants have their own independent controllable air feed mechanism. This independence is achieved by using different bellows 2272, 2274, and 2276 . . . . . . . , which forms a perforated floor 2270 at each step. Used in the vaporization chamber. The system of the carrying arms 22; 28, 2230 and 2232 of the mobile material in 2202 prevents entry and exit from the bottom of the steps 1 (2212 and 2214). Therefore, for these steps, the bellows 2272 and 2274 are slid from the sides. But the third stage bellows 2276 • . . " . . . . ' . ' .., .. · . · ...

Embedding, as shown in Figures 33 and 34. The hole-shaped top plate of the bellows 2722, 2274, 2276 in this design - ..... 23 02 (see also Figures 37, 38) is a relatively thin sheet with stiff ribs. The vein or structural support 2304 avoids buckling or deformation. In order to minimize the pressure of the flat front and bottom sheets of the bellows, a hole-shaped mesh is connected between the two sheets. "In order to allow thermal expansion in the bellows, only one side is connected, and the other three The side can expand freely. As shown in Fig. 37, the fixed sides of the steps 1 and 2 and the bellows 2272 and 2274 88 200817501 are also the continuous points of the air inlet tube ms. Therefore, the flail, ...' ... .· , ; . ' . _ Flange 2 2 8 0 will be at south temperature 'and must be sealed in the vaporizer 2 2 0 • · · · . . .. on the cold side wall - use a shield, such as As shown in Figure 37, for this purpose... :. . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . ; . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . ....... Will produce: i 'the gradient of the monument', so any one that is free of this configuration is an excellent one, which is that it will not be stressed when the bellows is firmly placed in the key. The gap between the hood 22 82 and the inner tube of the bellows m2 is filled with an insulator to retain heat and ensure a temperature gradient. When the bellows is in its vaporization chamber, the panel opposite the air connection extends to the bellows and stays on the fire resistant shelf. This provides support for the bellows during operation and also acts as a seal. The function of the piece prevents the material from falling below the bellows. It also allows for free movement so that the bellows can expand, as shown in the figure. The downstream edge of the bellows is also treated in the same manner. The upstream edge of the bellows is an R elastic plate seal 23〇6 enclosed between the carrier arm and the top plate of the bellows MM. '.. - The wind I is connected to the hot air supply pipe by means of a horizontal flange. Therefore, it is only necessary to separate the flange to remove a bellows. The second stage bellows 2276 is advanced from the bottom and is also sealed and positioned to the carburetor 2200 using a shroud. / # Avoid the dust falling on the edge of the third stage bellows 2276. The seal is hunted by a refractory protrusion that makes it set at the edge of the second stage 2214. The special edge can be sealed with an elastomeric seal projecting from below the recess in the side of the refractory. These seals are disposed on the upper surface of the bellows to seal between the side walls and the bellows. The downstream edge of the bellows is sealed by a bomb: a sealing member to a side of the uncased side, and the reinforcing member and the hole-like mesh between the flat surfaces of the bellows are thinned to make the bellows Sheet metal can be used. / Can be removed after separating the pipeline flail, -·· · . ' -.., ; - . ..: :, .\ . ' ' . . . See Fig. 42, using a series of carrying arms 2228, The 22 仏 system ensures that the MS W is moved laterally along the vaporizer 2200: the residue in each of the third steps 2212, 2214, and 2216 is moved to the residue out of α: 2208. Each of the three phases is serviced by its own carrying arm. The carrying arms control the pile height of each stage and the total indwelling time in the vaporization chamber. Each of the carrying arms is capable of moving through the entire or partial length of the step: at a variable speed. Therefore, the rung can be completely emptied if required. : . : ':· · ;: Each carrying arm contains an ampere-guided portion, a carrier arm with selective guiding portion, an externally mounted drive system and an externally mounted control system . The carrier arm design includes a plurality of false fingers ' such that the salt phase pore pattern can be configured such that operation of the carrier arms does not interfere with air passing through the air holes. In a multi-finger carrier arm design, the carrier arm is a structure in which the fingers are coupled to the carrier arm body, wherein the individual fingers have different widths depending on the position. The gap between the fingers in the multi-finger bearing arm design 90 200817501 is selected to avoid reactive material particle bridging 1 of the individual finger systems from about 2 to about 3 pairs wide, about 0.5 to about 1 inch thick And there is a gap between about κ and about 2 吋 wide. -.... ... The bellows pattern is configured so that the image interferes with the air passing through the holes. For example, when the pattern of the pores is hot, it is between the fingers (in the case where the seams are offset from each other: some holes are not covered and the other holes are covered)贤, • · · · ' ' '; . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . The factors include avoiding the fluidization of the bed. · ·························································· Along with . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . · '·. . . . . . ... to the nominal particle size (2 pods) to ensure acceptable kinetics. / · .* · ' . ·.,. , . , _ _ · · · * The multi-finger carrier arm can have independent built-in elasticity, so each finger shape can more closely conform to any undulation of the top surface of the bellows / . . . . This conformity.' · .. . V . . . . *· . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . The carrier arm is provided on the main bracket, which does not tighten the finger. This concept • * * ' · . , . . . . - ' * also allows the fingers to be easily replaced. The end of the finger is bent down to ensure that the tip contacts the top of the bellows when the relative position of the carrier arm and the bellows changes (eg, because of expansion). This feature is also reduced because the air hole is covered by the carrier arm to the process. Any harmful effects, air will continue to flow through the gap between the carrying arm and the bellows. Referring to Figure 39, the guiding portion includes a pair of substantially parallel elongated roads mounted on the frame at approximately 91 200817501 level. 2240(a), 2240(b). Each track has a substantially L-shaped face. The moving element includes a carrier arm body 23 26 and one or more elongated, substantially rectangular carrier arm fingers · * _ .. 2328, which is tailored to slide through the side walls of the corresponding vaporization chamber. ' ... . . . . * .'* , . . · · . .·_-- . . · . ' · . . · ..mouth;. .... ...· · ·· - · · · · · ···· .. . . . . . . -,... ......' · ...................... The carrier arm fingers are utilized Suitable materials are bound to high ^, . . .::.......············································································· The words are well-known: and can contain stainless steel, or mild steel, or; ^ 咏 ... · -... . . . Soft steel. Selectively, specific individual qi. . . . . . . . . . . . . . . . . . . . . . Alternatively, cooling can be provided in the reading fingers: arm fingers from the vaporization chamber 22〇2. * . . . * * . ι· . _ . '· · : . . . - . _ , , . . . * Externally circulating fluid (air or water) within the arm fingers. . . . The carrier arm finger dance is adapted to be sealingly engaged with the side wall of the Ί 化 。 。 。 。 。 。 。 。 。 。 。 。 。 。 。 。 。 。 。 。 。 。 , this will interfere with the process or can be ..... . . . . . . . . . ... can produce an explosive environment 1 also need to avoid harmful toxicity and flammable gas from - - . . . . · ·: - The vaporization chamber 2202 escapes and the excess of the residue leaks out. The oxygen can escape to the surrounding environment by accommodating the bearing mechanisms in a sealed box. The box has a nitrogen purge facility to prevent the explosive gas mixture from forming a residue seal in the box and restricting the gas seal to each finger of the carrier arm, using each finger pressed against the carrier arm The elastic strips 23〇8 on each surface are as shown in Fig. 4. Or, the Φ seal may be a packing gland seal that provides a gas and residue seal for each of the fingers. The seal design provides a good gas for each of the load bearing fingers and 92 200817501 wreck seal, the same睁 Do not interfere with the vertical and horizontal movement of the carrying arm. The sealing of the sides of the fingers is the greatest challenge as it must conform to the vertical and lateral movement of the fingers while maintaining close contact with the seal of the carrier arm and the upper and lower surfaces of the carrier arm. . You can use the window located in the sound of . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . In addition to the facilities. This removal can be done without destroying the shoulder ... , *. . . . . . . * t -·. . .

Completed under the body, such as the 4L.:................. .. ..., : The wide monument 2 3 1 0 package order has a dust The exit ^ j 23 I2 is equipped with louver 23 Ι ό and dust tank 23 3 factory 23 18 and a manual, chain 2320 driven duster 2322. When the operating lever 2 3 2 4 is used, the dust is pushed to the dust by the duster 2322. ώ·π 2314.0. The power of moving the kit carrying arms 2228, 2230 and 2232 is provided by the electric motor, which is transparent The gearbox and drive chain system drive the carrier arm. Briefly, the power to drive the talker arm along the rails is provided by an externally mounted electric variable speed motor 2256 that selectively drives the motor launch lever 2 25 8 ' in the forward or reverse direction. The carrying arm can control the rate to extend and retract. Position sensor 2269 transmits the carrier arm position information to the control system. Optionally, the motor can further include a gearbox, and two driver sprocket gears 2260 are mounted on the motor wheel. The drive chain 2260 and the corresponding driven chain 2262 mounted on a shaft 2264 are operatively engaged with the chain member 2266, which is secured to the elongated rectangular block 2244 by a bracket 2268. These motors are controlled by integral system control equipment that can command 93 200817501 opening and stopping positions, moving speeds and moving super apricot arms. In this implementation, the drive train is used to independently control each and to withstand harsh operating environments. For the purpose of maintaining the shoulder alignment of the carrying arms. When returning the carrying arm, the bearing and the cutting arm are not required to be precisely guided by the pouch, and the lowest hard arm 2232 is first extended, then #ϋ丄r Push the material down to the lowest carrying arm 22 ^ 〆 ^ 私 公 八 尽 232 232, fill the gap created by the movement of the carrying arm; talk about the minimum commitment to planting 2232 and then shrink: back; The upper carrying arm 2228 then extends to fill the intermediate bearing:] the gap behind the carrying arm 2230. Next, the intermediate carrying arm 223 is returned. ', the material is dying ^ ^ New from the 谲 feed 埤

The crucible fills any voids of red/i:V on the upper carrying arm 2228 and then makes 28 back. All of these actions: Known' The control system responds to system instrument data automatically and independently. : .* * · · See Figure 42 for the implementation of a cross-border 蚤 兮笙 儿 儿 曰 曰 曰 曰 曰 曰 曰 是 是 是 是 是 是 是 是 是 是 是 是 是 是 是 是 是 是 是 是 是 是 是 是 是 是 是 是 是 是 是 是The chaos is fixed (using the adjustable set point), and a small area is generated at the beginning of the step C2216; . . . · ·, the carrying arm B 2230 is immediately after the launch arm IC 2232 passes a starting distance In (starting distance ancient ^ sleeve # has adjusted adjustment set point). Carry arm Β 勋 / c 2216 domain. The feedback control is extended to the desired maximum distance to block the liquid level 217 or to minimize the set point distance, if it has been blocked, 94 200817501

Or maximize the set point distance V. If no blocking occurs. While the carrying arm B 223 〇 fills the small area at the beginning of the step C 2216, • · · · ... * · . . . . . . . . It also produces a small area from the step B 2230. • ... * - .... ....:. . . . . ..... * · , . . . -. .. ···: ·. . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . Carrying arm: A 2228 pushes/carryes the material to fill the stage immediately. . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . Small area '. The feedback control is Zhongchang to the fast; ·;. r ·; ; ··· .· , :' f distance to block the liquid level switch B Ml5, or t · ·. distance, if already broken, Or maximize the set point distance, if not • ·..· .... 'In, .... ... There is a blockage. In the carrying arm 2228: filling the step B 2214, ... ..... The resulting area creates a small area, which typically causes the feeder to operate and fill the vaporizer 2200 until the level switch A 2213 is again blocked; . . . . . . . . . . . . . . .. ...... . . , . . . . . . ' . ' All the carrying arms are simultaneously retracted back to the starting position. • . . . * · ' ' · · · ' ' . . ' ' · * — , ..... .. · .: The inlet and outlet of the vaporizer 22 are supplied by a manifold at one end. During operation, the seal can be closed by using a sealable refractory lining. Further access is also possible. This can be done by moving the third step windbox 2276. • The remaining residue (such as coke or ash) must be removed from the vaporizer 2200, and 1 |# sand is sent to the residue. Adjustment system (RcS) 4220. After the material is processed and moved in the /Lizer 2200, the heat generated in the pile can be melted, which causes the residue to agglomerate. The residual of the agglomerate has been shown. Things will fall off埠★认山, the style of the outlet is blocked. In order to ensure that any agglomeration will not be 95 200817501 . . . , .. - : . . . at the outlet of the vaporization chamber 2202 caused a blockage, using a screw conveyor 22〇9 The residue is taken from the vaporization chamber 2 2 〇 2. The movement of the carrier arm pushes the residue . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . · , .... .... · . . . . . . . 22 02 02 22 22 22 22 22 22 22 22 22 22 22 22 22 22 22 22 22 22 22 22 22 22 22 22 22 22 22 22 22 22 22 22 22 22 22 22 22 22 22 22 22 22 22 22 22 . - :, .. :. ' · · ·.. The rotation is in the residue: the material is sent to the conveyor system before it is released.

The scattered action system is based on. Located in the dryer screw snail I. · - · - * .. · - * * . ' ·· . _ · :' · .... ..... ·.,- ...... .... · . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . , must: all kinds of parameters in the steaming room 2202. / V - ;. "·:'. ·:;; V ' / : ;·. ; . '· ' ";. 々. For example, it must be at a different point along each step and each one. . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . ... .. .,.. Monitor the temperature at each level of the step. This is done by using hot work, which is in . . . . . . . . . . . . . . • The tendency of women to change during operation. In order to complete this process without stopping the process .... 'V · . . . . . . . . . . . . . work, each thermal light is embedded in the vaporization chamber through a sealed terminal tube L. , . _ . . . . . . . . . . . . 2202, which is then sealed to the container housing. This design allows the use of a flexible, ..., - . . . . . · flexible wire heat box, which is longer than the sealed tube, so the heat is light, ·:· ' :- /· · . · . . . : . . . . . The connection point (temperature sensing point) will be attached to the end of the sealing tube to ensure the temperature.. · .. . . . . . . . . · '. · Change the accuracy and speed of the response. The sealing tube is sealed on the vaporization chamber 2202, and the mechanical seal is held in place, which can also accommodate the protruding adjustment into the vaporization chamber 2202. In terms of temperature measurement within the MSW stockpile, the sealed tube may limit it to the V when it has to be moved. To avoid this problem, a deflector is placed at the end of the sealed tube to prevent the MSW from being The thermocouple tube is blocked. The outgas generated in the vaporizer 2200 is then moved into the gas recombination system (GRS) 3 200. The GRS 3 200 is designed to meet a wide range of requirements: (a) provide the necessary capacity for the required gas refining retention time; (b) provide insulation for 96 200817501 and insulation of the external steel container; (C) provide add (d) enabling the gases to be mixed; (e) using the plasma torch '3208 . . . , . . . . . . . . . . (f) For process control. And to strengthen the pulverized coal · . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . ^ Μ ^ ^ ^ ii . . . * · * . - . . , ' * '' The passed gas to the downstream heat exchanger 5200. . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . ....... ' ' ··.;·· ; ........ . . . . Process air, steam, plasma torch 3 2 0 8 and torch processing: mechanism , the instrument is .... "... . -·: and the installation of the discharge valve gas f GRS 32〇0 comprises a substantially vertical mounted refractory-lined cylindrical or tubular weight: group chamber 3202, which owns The car has a conical trapped inlet 32〇4, and the vaporizer 2200 has a length to diameter ratio of about 3:1 through the mounting flange 3214. The indwelling time in the GRS 3200 is 疋1.2 seconds. The GRS 3200 also includes three layers of tangential air jets.. . . . , . . , , nozzles, two tangentially disposed plasma torches 3208, six thermocouples, two combustions: ... ·. . . . . . . • • 埠 两个, two dynamometers 埠 and several spare 埠. The high temperature generated by the plasma torch 3 2 〇 8 in the GRS 3 200 ensures that the molecules in the outgas are decomposed into groups, and the elements are combined to form a syngas. The hot, raw synthesizer exits the GRS 3200 through the syngas outlet 3206. - . . . , . . . As previously stated, the GRS 3200 includes a support for a bonfire. The primary support feature for the firewood is a series of pickers 3222 that orbit the interior of the GRS 32. In operation, these shelves 3222 will be at a much rainy temperature than the housing of the recombination chamber 3202. Therefore, any waste of heat must be prevented by leading to the grs 3 200 while providing room for differential expansion. In addition, the shelves 3222 must be capable of supporting a substantial weight of the refractory. This 97 200817501 . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 'Knife and fork gap to avoid # 偟趴 叹 搁 搁 322 322 322 322 322 322 322 322 322 322 322 322 322 322 322 322 322 322 322 322 In order to carry the heavy shackles of the L ^ ^ τ coffin, one of the female shelf sections is supported by a number of gussets welded to the side wall #, as shown in Fig. 21. The prolonged blinks along the shelf 3222 are too a 〆 ♦ position:: The degree of swell is particularly stressful and may cause

The gusset plate is invalid, if it is 煜 煜 y _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ Repair, small on the middle gusset plate, then smash until only the outer part is welded. This minimizes any stress on the isosceles and possible bending of the thrower 3222. 32〇3, thus forming a sealed enclosure. The entire GRS woo is internally coated with a high-temperature resistant film to prevent the unsmoothed sesame rice from smearing on the outer surface of the apron to show hot spots due to refractory failure or other factors. · '..;:,· . ,..·.· . ... 1. ................:: The refractory material used is a multi-layer design with a high-density layer. The inside is resistant to the high temperatures, wear, erosion and corrosion present in the GRS 3200. The outer side of the high-density material is a lower-density material that has a lower resistance but a higher insulation constant. On the outside of this layer, a foamed sheet having a very low density with a very high insulation constant is used because it is not exposed to abrasion or ablation. The outer layer, between the foamed sheet and the steel shell of the container, is a ceramic full covering material to provide a compliant layer to permit differential expansion between the solid refractory material and the outer shell of the container. The compressive refractory layer separation zone of the incompressible refractory material provides vertical expansion of the refractory material. The compressible layer 98 200817501 is protected from the rice by overlapping but extendable high density refractory materials. As shown in Figures 48 and 49, the air system is injected into the airflow using a three-layer air nozzle, which contains four: the injector is in the lower layer, and the other six. - ; ... v .... ' ' · The body is in the upper layer, and the three injectors are slightly more than the other three injectors '·„········; : , ..... high to form the horizontal flow (cross- Jet) Mixing effect to achieve better mixing. Will: Air entertains the GRS 3200 at an angle, and the use is also in the future. Λ ..... . . . . . . . . . . . . . . . . . . . . . . ' . . . . . . . . . , 瑞 , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , ..... :. . , ' ' . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . .... Group room 32〇2 bottom Zheng used to make light air speed · induced vortex motion f gas gas system through the full 埠 3212 into the escaping airflow, in the scales turbulent flow .... .. .... . into a full motion or full flow, so mix the outgassing and read in the GRS 3200: Circulating eddy current pattern:: .. . * ... ' . . . · As previously stated, the GRS 3 00 also includes two tangential mountings mounted on a sliding mechanism.. . . . . . . . . .300 kW, water-cooled 'copper electrode ~: ^ Dingba to nitrotriazole gas-base tetrazolium) DC torch 3208, as shown in the figure. The straight • · : - - * * . • The current torch 3208 is powered by a DC power supply. The thermocouple is placed at multiple locations within the GRS 3 200 to ensure the syngas. The temperature is maintained at approximately 1000 ° C «The plasma 3208 requires weekly maintenance, and it is most desirable that they can be replaced while the process is still operating. As previously stated, this implementation uses two electricity in the GRS 3200. The slurry torch 3208, when only one operation is required. The shirting and replacement of the plasma torch 3208 must be completed in the presence of high temperature toxicity and combustible gas in the GRS 3200. In addition, the electric torch 3208 is in the plasma 99. 200817501 When the torch cooling system fails, it will also need to be removed to protect it from the thermal damage in GRS 3200 .* ' ——· .... . . * . The plasma torch 3208 is mounted by a sliding Huai plasma torch 3208 is moved out of the reformulating chamber may be configured to meet up. The plasma torch 3208 is sealed to the recombination chamber 3202 by a sealing glatid. This is also blocked by the 翁 箸 gate valve, #转到安装 and sealed in the I ^ ^ .................., ..· · . . . . . ,·+ . . : .. . Remove the torch 3208 and pull it with the sliding mechanism? . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . The initial movement of the piece is safe. ....... ..: . . . . . . The torch power supply is stopped. Operation. The gate valve is retracted through the torch 3208 through the... ..................... The valve automatically closes and the cooling cycle is terminated. Separate the teach and wire from the torch 3208, loosen the seal from the gate valve, then The electric torch 3208 is lifted off by the lifting device. . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . The torch 3208 is lost in depth. . . . · For the sake of simplicity and safety, all the above operations, except for the closing and closing of the gate valve, are performed manually. The brake is mechanically operated, so the operation is automatic. ·····... * : · · · · · · · · Use a pneumatic actuator to automatically evacuate the power when the cooling system fails • · · · · Torch. Used to operate the actuator Compressed air is supplied from a designated air storage tank, so the power is The same air storage tank is available at any time, even in the event of a power failure. Air is provided for the gate valve. An electrical joint cover is used as a further safety feature to prevent access to the high pressure plasma torch. 200817501 铨 铨 调整 ... ...... ...... ...... ...... ...... ...... 。 。 。 。 。 。 。 。 。 。 。 。 。 。 。 。 。 。 。 。 。 。 。 。 。 。 。 。 。 。 。 。 。 。 。 。 By taking it from the vaporizer 2200 into the electrical system residue

Adjusting chamber (RCC) 422〇:, dazzle it and make it into an emotional vitrified slag 42〇3, before transporting the rabbit slag heap U. Lishengping bucket: 424〇 cooling and powder bee melting Voucher. The final tantalum product is suitable for use in paving or concrete making. It becomes complicated because the heat generated in the pile causes agglomeration. Also suck ^, '··. * . . . . t ' .. . . by the use of the >Vizer i200 exit end screw-type transmission. Talk: The transfer article has a wrap-like edge on the screw thread. Then use the main conveyor 421 containing a series of screw conveyors. • . . . . . . .

The system sends the residue to RCC 4220. This conveyor system 421 is also from GCS. " . . .

The residue is taken downstream of the bag filter 6230 and sent to the RCC 422. In order to minimize entry into the RCC 422, residues from all sources are combined prior to passing into the RCC 4220. This avoids increasing .··:.-.. .... . ‘·.- .· ',. RCC 4220 to meet multiple feed sources. It may also be necessary to meet the source of the residue outside the amount. In order for vaporization to continue while the RCC 4220 is shut down, the residue can be transferred. In this case it must be re-imported into the RCC feed system. A complete overview of the residue adjustment system is shown in Figure 26. As shown in Fig. 54, the residue is taken into the ruler (: (: 4220) and accumulated therein in a storage tank 4222, the depth of which is determined by the height of the baffle 4224 and is heated by the plasma torch 4230. As the water level of the molten slag in the storage tank 4222 increases, it goes beyond the barrier: 4224 and falls into the quenching barrel 424. The water residue 4240 ensures that the RCC 4220 is sealed from the environment. • . . . · ' · · Any metal removed during the MSW processing system phase is transferred to the RCC. _ ·. . . . * '· - t 4220 'and not necessarily at the normal glass transition temperature of the marry residue Lower melting v so 'melting pot can: can be blocked by metal, because the A density is higher than the melting slag ^ no scales to avoid this phenomenon, periodically rises: after the 'construction of the metal; · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · In order to be able to marry the residue (transfer: it is its grandson ί often high: the temperature contains rot and know: ........ The refractory material will suffer from very harsh operations.) These ones. · · * *

Money is especially at the Rongcui waterline. In addition to the high temperature I In addition, the refractory material must provide good insulation to preserve heat, and the RCC 4220 must: :: 偻 may be small. The enamel material is selected to provide very heat-resistant, ... : : . . . . . . The internal lining of the anti-corrosion and Wei Qian, the refractory layer on the outside of the lining is then selected to be soft. Insulation β . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . The bottom of the RCC can not interfere with this... '.. ' ' . . . * :, Women. ··.. · * . Where is the RCC removed?' This is by The RCC is suspended from the support structure 4270 instead of being placed on a structure, as shown in Fig. 57. So the lower half of the rcC with the melting pot can be detached from the upper half without the need to separate any joints? In addition, the entire RCC can be removed by separating the connections and lowering them. This avoids the need to lift the conveyor belt 4260 and the pipeline away from its path. When the molten slag falls into the quenching barrel 4240, it is cooled and pulverized into fine particles. A slag conveyor 4260 then will be fine-grained slag 4203 102 200817501 . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . The quenching bucket 4240 is removed and placed into the stock pile 42〇4 for processing or further use, as shown in Figure 3. The meltdown is a good thing. . . . , . . . . '

The trap is separated from the environmental seal by a shield that is capped on the RCC 422 and whose lower edge is immersed in the quenching medium. The same quenching agent will seal off the transmitter 4260 and RCC 4220. V is generated in the RCC 4220 as a system and in the heart, . . . . , . . . . . . . . . . . . . . . . . . deal with. The shoulder residual gas is transmitted through ^ ^ 4228 m M RGC ; 4220 - M JL ^ ^ ^ ^ v (RGCS) 4250. It is pre-cooled in a sputum air-passing device by removing the granules and heavy metal contaminants. The first sub-heater "receiver 4256 is then used to cool the heavy metal and particulate matter before the heavy carbon and particulate matter is removed." The cooled and adjusted residual gas is cooled. Transfer back to the downstream. . . * * * GCS 6200 to feed: return the syngas from the converter 12 。 · ' . * . * The original synthetic 氡 leaves the converter 1 200 and passes a syngas pair. · · · · · · · · · Air Heater (HX) 5200 'here heat from the syngas stream to the air, flow. Therefore, the synthetic gas beer is cooled at the same time The hot air stream is fed to ..... . . - back to the converter 1 200 as process air. The cooled syngas then flows into..*, a gas conditioning system (GCS) 6200, where the syngas is further Cooling and sequentially removing particulates, metals, and acid gases. The clean and conditioned syngas (with expected humidity) is stored in the syngas heat exchanger (HC) before being fed to a gas engine 926 that produces electricity. Within 7230. Major zeros within the system after the converter 1200 and RCS 4200 Work element (device) can be summarized in Table I, in accordance with the order of processing of synthesis gas. 103200817501

Table 1 Converter 1200 and RCS 4200 Subsequent Step Subsystem or Equipment Main Function Heat Exchanger 5200 Cooling Syngas and Recovering Sensible Evaporative Cooler 6210 . - * : .* · * Further cooling of syngas before the filter bag Injection system 622〇 Heavy metal adsorption filter bag 6230 V Particles or dust collection, · . . . * Hydrogen chloride scrubber name 24〇—~~~ ~~—----: Remove the hydrogen-hydrogen synthesis gas cooling/adjustment Whole: Carbon filter bed 6260 Further removal of mercury: , Hydrogen sulfide removal system 6270 Removal of hydrogen sulfide and elemental sulfur recovery RGCS 4250 RC0 outgassing and cooling synthesis gas storage tank 7230 Synthetic chlorine storage and homogenization Reducer 7210; Gas/Humidity Control Liquid Separator 7220 • ': Eight...'乂. . : Gas Engine 9260 ' . . .. '...· . . . · Main Power Generation Drive Burner 9299 Burning syngas at the beginning

The synthesis gas to air heat exchanger (the recuperator V exits the synthesis gas from the GRS 3 200 at a temperature of about 900 ° C to 1100 ° C. In order to recover the thermal energy in the syngas, the raw syngas exiting from the GRS 3200 is Send to the shell-and-tube syngas to air heat exchanger (HX) 5200. The air enters the HX 5200 at ambient temperature, ie from about -30 to about 40 ° C. The air is circulated by the blower 5210 and is 1 〇〇〇 Nm3 The rate between /hr and 5150 Nm3/hr enters the HX 5200, usually around 4300 104 200817501

The rate of Nm3/hr. The syngas travels vertically through the tube side 5202, and the air flows through the shell side 5206 in a counterclockwise direction -. . . . . . . . The temperature of the syngas is reduced from 1000 ° C to 500 ° C and ........... · · 8001 C (more than about 7401), while the air temperature rises from the ambient temperature. ................... Up to between 500 ° C and 62 5 ° C (preferably about 600 ° C). The hot exchange is empty.. ; :·· .: . . . . . . . . . . . . . . . . . I loop back to the converter 1200 for gasification. • · · · · · · · · · · . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . ·········································.. - · · · The flow of syngas and air (5) is designed to minimize the accumulation or erosion of particulate matter, · · · · - . . . . . . * * . : * ..*- * - - The area that can occur. In addition, the gas velocity is designed to be high enough to automatically clean while still minimizing erosion. Because of the significant temperature difference between air and syngas, the HX 5200 has a separate expansion tube 5222 for each line 5220. This is to avoid ''.. . . . Pipeline break: crack is indispensable, pipeline breakage can be very dangerous: '. . . . * .. because air will enter the syngas mixture. When a single pipeline is blocked by . . . . . . . . . . . . _ :.. and can no longer expand/contract with other bundles, the possibility of pipeline rupture: - ... · ( * .... · · · · ..................... Sex is very high. Multiple temperature transmitters are set. In this gas-to-air heat exchange '.....--.. . . . _ _ - 5200 on the gas output box. These are used to detect air leaks to the . ' . . . . . . Any possible temperature rise caused by combustion. The fan 5210 will automatically shut down in this case. The material used for the air pipe in the HX 5210 must be carefully selected to ensure that no corrosion problems occur because of the syngas Internal sulfur content and its concern at high temperatures. In our implementation, alloy 625 was selected. 105 200817501 Gas Adjustment System (GCS): . -... '·· . . . . . . ... · · · · · · · · · _ . In general 'gas adjustment: Fenghua (GCS) 62 〇〇 represents a series of steps that convert the raw syngas obtained after heat exchanger 5200 Suitable form for downstream dance applications Meals.... . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . (b)|Form (for particle transfer by mass metal transfer ^ ^ II 6240 ; (e) ^^ ^ (Μ ^ Μ Μ 62 5 0 ;/(f)^ i§. Ferry (% machine) 6260 ; (g) Hydrogen sulfide (sulfur) removal system: and (h) use desuperheater 7210 and gas / liquid separator 72 ^ .. . # ' . .. system.

: ... ' . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . The gas) blower 625〇 typically includes a gas cooler 6252, which is sometimes separated from the phase 2 of the GCS 62〇〇. In addition, the humidity control referred to herein as part of Gcs 62〇〇 Phase 2 is often considered to be part of the Syngas Regulation System 7200 further downstream of the GCS 6200. ... · · Figure 59 shows a block diagram of Gcs 62〇〇 implemented in our system. This is also an example of a bar-making process in which GCS 6; 2〇〇 is integrated with rgcs 4250. Figure 60 shows the layout of the GCS. After the initial cooling in the hot parent exchanger 5200, the input syngas is further cooled by dry quenching, which reduces the syngas temperature and also prevents condensation. The use of an evaporative cooling tower (also known as dry quenching, 621) is accomplished by injecting water directly into the gas stream in a controlled manner (adiabatic saturation). Water is atomized at 106 200817501 before it is sprayed into the air stream. Since there is no liquid present during cooling, the process is also referred to as dry quenching. When the water evaporates, it is combined with * * . * ... .

The gas is absorbed into the heat, so the temperature is lowered from 74 ° C to 15 ° and 30 (between about 250 deaths). Increase the control to ensure that the water does not exist. .... in the gas. The relative luxury at the temperature of the oxygen discharge, therefore you are low.....··· . . . . . - - . * . . . Steaming, hair cooling tower 6 2 1Q, f .- . . . . . . . . . . . . . . . . . . . . . : * : : : : : : : : : : : : : : : : : : : : : : : : : : : : : : : : : : : : : : : : : : : : : : : : : Surface adsorption caused by the destruction of macromolecules. . . . . . . . . . . . . Osin. Therefore, most of the heavy metals in the gas stream (mine, wrong, mercury, etc.) and its. · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · , .. · The complex granules and then return to RCS 42 〇〇 to proceed to one: the step of the man back... .: , ' ..... Receive, as described in the next step of the apricot In order to obtain effective adsorption, it must be 蟢 . . . . . . . . . . . . at the stage of the synthesis gas has sufficient retention time, can also be dry injection here * * Stage 6 2 2 0 use other Materials 'such as feldspar, lime, and other absorbents, · . . . . as activated carbon, or in addition to activated carbon, to capture the weight within the syngas......... .. metal and tar, and will not block it. Then remove the particulate matter from the syngas stream in the bag filter 6230. * * and have the activity of heavy metals on its surface, with extremely high efficiency The operating parameters are adjusted to avoid any water vapor. Condensation. All particulate matter removed from the syngas stream forms a doughnut that further enhances the efficiency of the filter bag filter 623. Thus, although the new uncovered bag has 99% removal efficiency, but the filter bag filter 6230 is typically designed for 99.9% particulate matter removal efficiency. The bag filter 6230 uses a lined fiberglass bag, an unlined fiberglass bag or P 8 4 basalt bags, and at a temperature of 20 (TC and 260 ° C) 107 200817501. When the pressure drop across the bag filter 6230 increases to a certain set limit • . . . . . . ........ .. degrees, use a pulse of nitrogen to clean the filter bag. For safety reasons • . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . ... and sent to the residue adjuster 42Q0 for further conversion or processing. • \ . . . . . . . . . . . . : : : : : : : : : : : : : : : : : : : : : : : : : : : : : : : : : : : : : : : : : : : : : : : : : : : : : : : : : : : : Figures 63 and 62 are differentiated • · · . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . '; : . .1 ; 乂..·':: The general wife: Figure... and ^ set:: meter..... ^ : · . . . · · C > · The bag filter uses:: A cylindrical filter that does not require a fulcrum. . . . . . . . The bag filter: Typical operating specifications for <230 (assuming the input is ash: · * ' · · * - ... and heavy metals) as follows: ^ Long designed air flow rate 9500 Nm3 /hr Bauxite load 7.4 g/Nm3. Cadmium V: 2.9 mg/Nm3 False 106.0 mg/Nm3 Mining · 1.3 mg/Nm3 Filtered filtration system output ·· . . . . . . . . * * Particulate matter 11 Mg/Nm3 (about 99.9% removed) Cadmium 15 /zg/Nm3 (about 99.65% removed) Lead 159 # g/Nm3 (about 99.9% removed) Mining 190 from g/Nm3 (about 90% removed) There is a large amount of heavy metal contamination residue 108 200817501 in the filter bag filter 6230. Therefore, as shown in Fig. 59, the residue is sent to the plasma base - - . . . . . . . . . . . RCC 4220 to be converted into glass: slag 4203. The second gas stream produced within the RCC 4220 is then processed in a different residual gas regulator, RGCS 4250, in the following Stage 1 process: in an indirect air pair. · · · · · _ . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . Concentrator 4254 * ·,.. - - · * .... . ;. A · , · . . - * ... Remove particulate matter and heavy metals. The smaller 啲篆.· . . . . ♦ · · · · ♦ Strictly used in the RCC 4220. - ... · · * ' . ' . . . . . . . Show that the extra steps of the RGCS 4250 politics include the use of _ * * . . . . ' 4256 it - # ^ «Ρ 13⁄4 ΛJi V ^ ^ I^r ^ . .. ·· · ·.

Genus and granules. The treated second syngas stream is then transferred back to the GCS 6200 to feed back the main input synthesis before the filter bag filter 230. . . . ': . , . . . . - Inside the airflow. · · · - - - - - · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · The filter bag filter 6230 is significantly less than the 'small filter'. . . . . . . The bag filter 4254 acts as a purge of the heavy metals. The amount of heavy metal that is removed from RGCS 4250 · .* · * .. * will vary depending on the MSW feed composition. It is necessary to clean the material to the hazardous waste treatment, when the heavy umbrellas accumulate to one finger - * · . . . - . . . V - . The following is a typical design specification for the smaller RGCS filter bag filter 4254. Again assume that the input is fly ash and heavy metal: Design air flow rate. 150 Nm3/hr Dust load 50 g/Nm3 440 mg/Nm3 109 200817501 Wrong 16.6 mg/Nm3 Mercury 175 mg/Nm3 Guaranteed over-burden system output: Particulates plant ^ 10 rrig/Nm3 (about 99.99% removed) Cadmium lead ' Mercury 166 "8/]^1113 (about 99,999% Xu) · : ' . . . . . 乂. 1 7:5 : /τ g/Nm3 (about: 9 9 · 9% lighter) . . ....... .-

The GCS 6200 can contain both direct and indirect feedback or monitoring systems\.. . . . . . . . . . . . . Our real/application, GCS and RGCS filter bag filters: both have dust The induction benefit is at the outlet (direct monitoring) to inform the filter bag from rupturing. If the bag breaks, the system is closed for maintenance, and optionally, the water flow in the hydrogen chloride scrubber 6240 can be analyzed at startup to confirm the micro-surface removal effect. The rate of nr from the bag-passing device 6230 leaving the particle-free synthesis gas stream in a fill: · ..... ... ... in the charging tower scrubbing, using a recycled alkali solution to remove any chlorine present • · *- .. . Hydrogen. Hydrogen chloride scrubber 6240 also provides sufficient contact area to cool the gas to about 35 °C. A bed filter 6260 is used to separate the liquid solution and possibly soluble water contaminants such as metals, hydrogen cyanide: ammonia, and the like. Hydrogen chloride scrubber 6240 is designed to maintain an output hydrogen chloride concentration of about 5 ppm. A wastewater discharge stream is sent to the wastewater storage tank 6244 for processing. For metallurgical considerations, a hydrogen chloride scrubber 6240 is disposed upstream of the blower 6250. An example schematic of one of the cesium chloride scrubbers 6240 containing associated components, such as heat exchanger 6242, is shown at 64. 65th icon 110 200817501 An exemplary system for collecting and storing wastewater from GCS 6200. A hard bed. . . . . . . . . . . . . 6245 was added to the water flush (bl〇wd〇wn) to remove tar and heavy metals from the wastewater. The typical specifications of the hydrogen chloride scrubber 6240 are as follows: . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . design flow rate · ^ , 95 〇〇 Nm3 / hr brush: the normal input of the washer / maximum hydrogen chloride bearing 〇 · i 6% / 〇 29%. . . . . . . . . . . . . . . . . . . . Hydrogen peroxide output concentration into: ^ \ : After removing hydrogen chloride, like using a blower 625〇, it provides gas from the converter. 1200 through the entire system: 12 〇 to i no power 'The It fan 62 ~ is also upstream of the mercury machine 626 ,, because the latter. Under pressure, there is a sturdy spring removal efficiency of 6260 size. Sections G8 through 33 are schematic diagrams showing the positions of the entire system 12 and the process gas blower 6250. _ . . - . . . ' The blower 6250 is designed with all upstream container design pressure drops. It is also designed to provide the required pressure for downstream equipment pressure loss. To have a final pressure of ~2·1 to 3·〇 psig (usually 2.5 psig) in the HC 7230. Since the gas is pressurized as it passes through the blower 625, its temperature rises to about 77 C. The built-in gas cooler 6252 is used to reduce the temperature back to 35 C because the maximum operating temperature of the hydrogen sulfide removal system 627 is about 40 〇 C . . . . . . . The final refining equipment for any heavy metals remaining in the Syngas Tour. The efficiency is improved when the system is under dust rather than vacuum, at lower temperatures, the gas system is saturated, and when hydrogen chloride has been removed by 2007 200851 and therefore does not deteriorate carbon. This process can also be used to synthesize gas streams. • V ‘ . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . The carbon bed * . · - · · · · · · · · · · · Filter 6260 is designed for more than 99% mercury removal efficiency. ..- .. .... The performance of this system is measured by periodic analysis of mercury in the gas. Repair ........... is by adjusting the carbon feed rate and monitoring the ^ - * · · '· · · .... . . . And borrowing: from the mining: sample to analyze the efficiency of the double bed, :.......:, . . . . . . . . . . . . . . . carbon bed filter 6260 Typical specifications are as follows: • - · . . . . . '.":'· , . :" . . . . . . · ....... Λ . ' .. . ' ... ... . · · * Design airflow rate j 9500 Nm3 / hr Normal / 襄 large recording load V U90 from g / Nm3 / 1.3 mg / Nnl3; ', ·:..,. .. ..... .. · · · . . . Carbon Bed Life: Life: 3-5 牟 Note the carbon bed output: 19 from g/Nni3 (99%) .. ....... ·. .... · . . . . . . . . . . . . . . . . . . . The decarburization removal system 6270 is based on the Ottawa Environmental Protection Agency of Canada: . . . . The A7 guidelines outline the sulfur dioxide emission limits, which are said to be a month in the gas... The syngas burned in the engine produces a sulfur dioxide platoon below 15 ppm. . Put. The cyclization removal system 6270 is for the output hydrogen sulfide of about 20 PPm *.. . . - - . . . Figure 4 shows details of the hydrogen sulfide removal system 6270. Choose Shell Paques Biotech for the removal of 6270 from hydrogen sulfide. This technique consists of two steps: First, the synthesis gas from the carbon bed filter 6260 passes through a scrubber 6272 where hydrogen sulfide is removed from the syngas by a recycle alkali solution. Next, the sulfur-containing solution is sent to the bioreactor 6274 for alkaline regeneration, sulfide oxidation to elemental sulfur, sulfur filtration, sulfur, and discharge disinfection to meet regulatory requirements. The hydrogen sulfide removal system 6270 112 200817501 is designed for an output concentration of 20 ppm / . . . . . . . . . . . . in the bioreactor 6274 to make thiobacillus bacteria Sulfide is converted to elemental sulfur by oxidation with air. A * · ·. , - - · · . . . * Control system 8200 controls access to the bioreactor you ^ ... * . . ' - . . ' . Holding the sulfur stock in the system Secrets: 62? 6 over the slippery flow of 6274 (Chongchuanchuan ^ also).来^ .. · . . ' . . . . . . . . . . . . . . . . . . . . . . . . . . . . .

Emission sources:: A singular solid discharge of water with a certain I liquid discharge with sulphate, soil acid and cold biomass. Both rows are in the end: disinfection before treatment:. Typical specifications for the hydrogen sulfide removal system 6270 are as follows: .... 丨 Λ: Λ . . . . . . . . . . . . . . . . . . . . . . Rate 8500 Nm3/hr • ······ . . . . . . . . . . . . . . . * Normal/maximum hydrogen sulfide bearing 353 1) Yang / 666 1) 1) 111 Guaranteed 5 positive system vulcanization Nitrogen output 2 〇Ρ ρ Π1 . . . . . . . . . . . . . . . . . . . . . . . . . After removing hydrogen sulfide, let the deuterium cooler 7210 to condense the water out of the synthesis, .. . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . The device 7210 supercools the gas from 35 to 26. (: The water condensed from the input stream is removed by the gas/liquid separator 7220. This ensures that the gas has a relative humidity of 80% and is reheated to 4 after being sent to the gas engine 9260 after the gas is stored. It (engine demand). The following table provides the main specifications for the entire GCS 6200: 113 200817501 悴媳 Tower 6210: The gas is taken from 740 degrees in a 2 second residence time • · . . . . . . . . . Cooling to 200 picometers * . . . . ' Dry injection 6220, 90% mercury removal efficiency . . . . . . . . . . . . . . Filter bag filter 6230 : 99 ·9% particle removal efficiency: . . . . : ' ·. . . . . : . . . · 99.65% mine removal efficiency 99.9% wrong removal efficiency hydrogen chloride brush 6 2 4 0 99 ·8 % hydrogen chloride removal efficiency blower 625 0 no leak seal rotary blower. '..V..:......' . . . . gas cooler 6252 〇 ·5 MBtu/hr cooling load. ... · · . . . . . . . Carbon bed filter 6260 99% mercury removal efficiency • . . . . . . . . . . . . . . Brush 627Q in the scrubber out of hydrogen sulfide - 20 ppm .... ·_·.* ' .········ . . . Bioreactor 6274 Minimum regenerative maximum regeneration efficiency.... . . . . Filter press 6276 2 days sulfur removal capacity homogenization chamber 々 230 2 minutes gas storage Capacity·· . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . * * As noted above, the GCS 6200 converts the input gas into an output gas with the desired properties. Figure 33 shows the overall process flow diagram for the GCS system 62〇〇, which is tied to electricity. The slurry gasification system is integrated with the downstream application. Here, the first gas stream generated in the Rcs·4200 is fed to (^3 6200. . . . , . . . . . . . . . . . residual gas regulator (RGCS) As previously described, the residue from the GCS filter bag filter 6230, which may contain activated carbon and metal, is periodically cleaned with nitrogen and passed to RCC 422 0 'which is vitrified here. From RCC The 422 〇 gas is directed to 114 200817501 through a residual gas regulator (rGCS) 425 〇 filter bag filter 4254 to remove '. · - · . . . . , . . . · De-particles, and enter the activated carbon bed 4258 Former benefit 4256 cold .... .. ; ·..· ' But. The bag filter 4 4 5 4 is also periodically cleared based on the pressure drop across the system. .... ... ...... clean. The residue collected in the RGCS filter bag transition 4254 is suitably treated as - . . . . The flammable gas leaving the RGCS 4250 as the upper air stream is sent back to the main GCS 6200 to fully use the heat of recovery. · : · ' ..·/ · ...... .... ··· ,·· ·:::; - ·Λ···' , ' :- .·'·: ·. . . ·-.·\ ;· ·:·:;···';- w . · ································································ · .··· Syngas adjustment system clean and cooled syngas from GCS 6200 into syngas**.. " · * . . . . . . . * System (SRS) 7200, It is designed to ensure that it flows to the next · · * 9260's combined gas has a consistent gas quality. SRS 72 〇〇 Shape In addition to the gas composition (mainly its low calorific value - LHV) and the short-term change of its pressure ... ... -.. .... Although the downstream gas engine 926 will continue to operate and generate electricity, the LHV or pressure of the syngas has short-term variations, but it may be due to unhealthy combustion or poor fuel pairs. The air ratio is out of its threshold radiation limit. The SRS 7200 includes a desuperheater 7210, a gas/liquid separator 7220, and a homogenization chamber (HC) 7230. The gas is heated by the gas engine 9260 at the outlet of the first gas storage to meet the engine temperature and degree requirements. Two types of homogeneous chambers (HC) are available: fixed volume HC and variable volume HC. The latter is more useful in reducing flow rate and pressure variations, while the former is more useful in reducing LHV variations. Because of the nature of the msW feed, LHV variations are more pronounced in our applications. Mixed volume HC is also generally more reliable than variable volume in its construction and maintenance. Figure 42 shows an illustration of a homogenizing chamber (Hc) for use in the present embodiment. Its system 115 200817501 . · · . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . :. : ·. . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . The indwelling time depending on the gas analyzer S13 is usually true analysis and feedback >. Maximum detachment

All of them get 3% UHV changes, and the birds have a few minutes of storage. ♦ · · . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . · · · · · : The HC 7 2 2 Q is 2 · 2 to 3. 〇 ps) g ^ The fuel of the downstream gas engine 9260 ^ 'remains. The 7230 is designed for 5 psig of the gate to handle unusually excessive pressure conditions...............................··_. ..... . . . The 2 minute retention and time of HC 723 也 also provides adequate storage to reduce pressure changes. As far as we are able to set the leaves: words, the allowable pressure of the gas bow 〇 〇 〇 · · · · · · 力 力 力 力 力 力 力 力 力 力 力 力 力 力 力 力 力 力 力 力 力 力 力 力In the event that the downstream gas engine 926 fails, it may be necessary to buffer (depending on the control system's response time and the retention time of 3〇_S5 seconds) to slow down the process or burn excess gas. The syngas flow rate typically entering HC 7230 is ~8400 Nm3/hr. Because of this, the HC volume must be about 280 m3 in terms of 2 minutes of indwelling time. \ , . · _ .. . . . . , · HC 7 230 is free-standing and outdoors, where it is exposed to snow, rain and wind. Therefore, the dimensions of the HC 7230 are designed to meet mechanical engineering requirements. Its support structure 7232 is joined to the concrete foundation. * _ ·· · · Because some water will condense from the syngas, the bottom of the HC 7230 is designed with a bottom drain nozzle. In order to assist the HC 7230 in watering, it is intentionally not to design its bottom to be flat, but to have a conical bottom of the panel. 116 200817501 Use a tracking/insulation water pipe to form the drain flange. Because the water inside the HC 7230 ' * .* * · - · must be gravity drained to the floor drain, keep the HC 7230 slightly. * * - - ... · .

The HC7230 is designed to meet the following design requirements.

Normal / / λί inlet temperature * * ; / . . . · Normal / maximum operating pressure normal / ^ maximum intake flow rate .. · normal / maximum light oxygen flow rate relative humidity • . . . . · storage volume: mechanical Design temperature mechanical design pressure

3 5^/4010 · · . 1.2 psig/ 3.0 psig . . . .,. * 70 0 0 Nm3/ hrX 840O Nm3/ hr 7000 Nm3/hr/ 8400 Nm3/hr ** . . , . . 60% -100% 290 m3; _40lC to 503⁄4 5.0 psig Materials used for HC 723〇 must take into account the above mechanical design requirements and the following typical gas composition two to two from the & 丨 & & 呵 呵. Because of the presence of water, hydrogen chloride, and barium sulfide

In the case of corrosion, corrosion is a special consideration." 47.0 9% 7.44% 20 ppm 3.43% 18.88% 21.13% Nitrogen Carbon Dioxide Sulfurated Water Carbon Monoxide Hydrogen 117 200817501 : Methane 0.03% .... .. ... . ^ 5 ppm ...... ......._ .: . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . .... . · A J6 English leaf manifold, close to the bottom to close; ............................" ..... ·' ·.. ........ ' ― 6-inch flange, at the top to release pressure; :-' , :;·. ;:· ·.;;:'.· '· ··. /·' ·. .: ... a 16 pod violin flange on the outer casing for gas input; a 16 inch pair of convex lines on the outer shell to rotate the gas; ..... . . . . . . . ..*. ' - . ······ Six six-inch pairs of flanges on the outer casing (2 for pressure, •............ : . . . . . . . . . . . . . . . . . . . . Temperature and 3 spares) A 2 inch flange, at: HC bottom (drainage) ; and * . . . . ... a 1 inch flange on the bottom cone for the liquid to meet the design To the requirements, HC 7230 is also provided: an opening cover the manifold, and Perpignan blinded (blind flanges), ·; * spare nozzle... • . ' . . . . _ · · . . Ladder, allowing safe proximity (for example, with track) to the house · . . . . . . * . . . · · Required hooks and anchor bolts. Concrete annular wall. Internal and external coating of HC 7230, if required. Insulation and thermal tracking at the bottom of the HC 7230. Concrete slabs for support. The Gas Engine 9260 design requires the input gas to have a specified range of ingredients under the designation. Therefore, the use of the desuperheater 72 1 0 will be used for one of the pressure switches. For all:: top. and pressure relief relative humidity open fluidized nitrogen 118 200817501 Brush 6270 clean gas from 3 generations of subcooling to 2 generations / using gas / liquid separator 7220 to drop due to condensation of the gas stream Any water. This ensures that once the regenerative oxygen is reheated to 4 generations, it will have a typical requirement of 8% relative gastrain 9260. Use the drum machine 6250 to extract from the system: gas, by providing all equipment and tubes:: the appropriate road: suction r machine design attention to the project implementation of the good and the Standard and aSHA guidelines. The blower is volt, 3rd step, and 6 0 Η z. The blower 6250 is designed to meet the following functional requirements. .... ...

— :—~~ --:---- Normal gas entrainment temperature. .... ' . 3 5U Normal pumping pressure -1.0 psig Normal gas - Flow rate 7200 Nm3/hr ------ Maximum gas flow Far 9300 Nm3/hr Dare pumping temperature. 3 51C Normal discharge pressure 3.0 psig Normal discharge temperature (after gas cooler) <35〇C Mechanical design pressure 5.0 psig Gas relative humidity at blower inlet 100% Gas molecular weight 23.3 Cooling water supply temperature (product gas cooler) 29.5〇C Acceptable maximum gas discharge temperature (after product gas cooler) 40°C 119 200817501 Operating load shedding ratio (turn down ratio^^ ^^ ^ ^ 10% Typical draw) The gas composition (wet basis) is as follows: methane 0.03% . . . carbon monoxide 18.4%:: • - - · . * carbon dioxide 7.3 8% . · . : . hydrogen 2 0.5 9% normal / maximum hydrogen sulfide 354 / 666 ppm water 5.74% normal / ^ maximum chlorinated nitrogen 5ppm / 100 ppm nitrogen 4 7.8 5% Because syngas is flammable and explosively mixed with air, blast. · ·. ' ..' ...' .. .. .. .... . . Machine 62 50 is configured to make the pole sign to no air will be from the big Absorbed into::: - * * .......

Into, and very little to no gas; poor to the atmosphere. All working fluids, ie, the seal cleaning system, are completed with nitrogen and use a leak-free shaft seal. Use an advanced leak detection system to monitor bubble leaks in any direction. - - * . In addition to the above design criteria, the blower 6250 also provides: a P-popular motor with a leak-free blower shaft seal. Gas cooler 6252. A muffler with a muffler cover to meet the common chassis of the blower and motor with a humming specification of 80 dBA at 1 m. 120 200817501 Auxiliary hydraulic pump with λ violation, and all instruments required for the attachment system of the blower. • * . . . . . . . . ‘ . -, .. .. ·

All equipment and controls (ie, low and high oil pressure switches 'high discharge pressure I temperature differential, temperature difference and differential pressure switch). All switches across the discharge sound: meter, discharge thermometer net the same as the Heng, the green box wiring ' must and yFD is controlled by the ampoule: upstream pressure roller, .' -· ...; ;.;· :··;··. . ;;········.:·····::···: · · - ; - - · ' : Eight zero leakage discharge check 1 Prepare each system to prevent the blower from experiencing excessive power/1 shut down (for example, systems like PRV and recycling lines). : is ^ in . The drum machine 625 is configured to assume the following environmental conditions. Altitude latitude longitude average atmospheric pressure maximum summer dry bulb temperature design summer dry bulb temperature design summer wet bulb temperature minimum winter dry bulb temperature average wind speed maximum wind speed design wind speed 80 meters 45/24, N 75 °40VW 14.5 p si a 3 8 ° C 3 5 ° C 2 9.4 〇 C 36.11. . 12.8 ft/sec 123 ft/sec 100 mph/160kph 121 200817501 The heat generation varies between approximately 3000 and 33000 kJ/kg, and the HC has a 2 minute indwelling time and typically a pressure of approximately 210 mb ar. A variation of about +/- 60 mbar is possible without exceeding the minimum supply pressure of the engine of about 15 mbar. Without a control system, the pressure change can be as much as about 1 00 mb ar ' so the long-term flow rate change is actively reduced by up to 4 times (or 75%) by the control system to operate the gas engine 9260 under a fixed load of the pre-study. In addition, the pressure change of the converter gas without the control system can reach about 25 mbar/s ′ which is 2.5 times (or about 60%) of the maximum plant of this example engine of about 1 〇 mbar/s. Thus, the control system of the present invention can reduce short-term process variation by at least 2.5 times (60%) and reduce long-term process variation by about 4 times (75%). Using hc 7230 in this example can help reduce short-term variation. Embodiment 2 In this embodiment, another control schedule of the vaporizer system as shown in Embodiment 1 is provided. This control schedule is shown in Figure 73 and is another variation of the control routine of Figure 71, in which a synthetic gas pressure detection module is substituted for the synthesis gas flow detection module. Embodiment 3 In this embodiment, another control schedule for the carburetor system as shown in Embodiment 1 is provided. [FIG. 74 provides another control flow chart showing various sensed characteristic values, controllers (ie, The response element) and the operational parameters that can be used by the control system 8000 of the present invention, and the interaction between them, can facilitate the proper and efficient processing of the feed. In this embodiment: 144 200817501 The conversion stealing solid south degree detection module 8 5 5 0 is configured to control the transfer unit controller 8 5 5 2 'the system configuration to control the action of the transfer unit 8 5 54, And jointly controlling the total MSW + HCF feed capture rate 8550 for control; the syngas (product gas) carbon content detection module 8558 (eg, from the gas analyzer 8130) is operatively linked to the MSW: HCF proportional controller 856.0 To jointly control the total MSW + HCF feed rate f 85 56 to control the MS W/HCF splitter 8362 (to control the '.. 'MSW and HCF feed rates 8564 and 8566, respectively) and jointly control the transfer unit controller 8552 and total air flow controller 8574; ' * Synthetic airflow detection module 8572 is operatively coupled to a total feed controller 8596 for collective control of the total air flow controller 8574 and the common control total MSW + HCF Feed rate 8556; synthesis gas (product gas) fuel value determination module 8568 (eg, LHV-c1*[h2] + C2*[CO], where cl and c2 are constants, and [H2] and [CO] are derived from Syngas analyzer) and fuel: air ratio controller (8570) The common air flow controller 8574 is controlled to control the total air flow 8566 and the total MSW + HCF feed rate 8556; and the process temperature detecting module 8576 is operatively coupled with the temperature controller 8580 to control the air flow distribution 8582 And plasma heat 8854. Embodiment 4 In this embodiment, another control schedule of 145 200817501 of the vaporizer system as shown in Embodiment 1 is provided. Figure 75 provides another control flow diagram showing various senses The characteristic values, the controller (i.e., the response element), and the operational parameters that can be used by the control system 8000 of the present invention, and the interaction between them, can facilitate the proper and efficient processing of the feed. In this figure: The solids height detection module 8650 is configured to collectively control the transfer unit controller 8652, which is configured to control the operation of the transfer unit 8654, and to jointly control the total MSW + HCF feed rate 8656 'for control; syngas (product) The gas) carbon content measurement module 8658 (eg, from a gas distributor) is operatively coupled to the MS W: HCF proportional controller 8660 to jointly control the MSW/HCF separation 8662 for separately controlling the MSW and HCF feed rates 8564 and 8566; the syngas (product gas) [Hb] content detection module 8667 (eg, from a gas analyzer) can jointly control the fuel: air ratio controller 8670 To jointly control the total MSW + HCF feed rate 8656; the syngas (product gas) opacity detection module 8669 can be used to jointly control both the fuel air ratio controller 867 and the fuel: vapor ratio controller 8671; Syngas (product gas) [CO] content detection module 8669 (eg, 'derived from a gas analyzer) can jointly control the fuel: vapor ratio controller 8671 to jointly control the steam flow calculation 869 for controlling steam addition The rate 8692; δ into the airflow detection module 8 6 7 2 is operatively connected to a total air flow controller 8674 to control the total air flow 8676 and a total of 146 200817501 with the control total MS W + HCF feed rate 8656; And the process temperature detecting module 8 6 7 8 is operatively coupled with the temperature controller 8 6 8 to control the air flow distribution 8682 and the plasma heat 8684. Example 5 Figures 17 and 18 provide an illustration of how this control system can be used to control another process in which a carbonaceous feed is converted to a fluorocarbon. In this embodiment, the water is preheated into a vapor as an additive, the oxygen is preheated as an air force σ, and the carbonaceous feed is preheated as an air additive and fed. To a converter used for conversion. At the output of the converter, one or more sensing elements are provided for detecting the flow rate, temperature, and composition of the product gas. As shown in Figure 18, at the gas flow rate sensed. /〇(:〇 and %(:〇2 to estimate the carbon content in the product gas to adjust the feed rate of the feed. It can be further estimated by the induced %CO and %C〇2 and %Η2 The new 〇2 and vapor injection rate to achieve the desired gas composition 1 Finally, if necessary, the temperature of the plasma heat source can be adjusted to the level of the plasma heat source. All patents and publications referred to in this specification. , including the disclosure of the patent application, and the disclosure of the database registration are specifically incorporated by reference to the full extent of the same degree, as each such individual patent, publication, and database is specifically and individually indicated by The present invention has been described with reference to the particular embodiments of the present invention, and it is to be understood by those skilled in the art without departing from the spirit and scope of the invention. All such adjustments that are apparent to those skilled in the art are intended to be included in the scope of the following patent application. [Simplified Schematic]. Embodiments of the invention, by way of example only, and with reference to the accompanying drawings. Fig. 1 is a schematic diagram of a control system for controlling a vaporization process. . . . . . . , according to an embodiment of the present invention, the vaporization The process is carried out by a system that converts a charcoal-containing feed into a gas. Figure 2 is a schematic diagram of a system for converting a carbonaceous feed to a gas, in accordance with an embodiment of the present invention. In one embodiment of the invention, a schematic diagram of a system for converting a carbonaceous feed to a gas. Fig. 4 is a schematic illustration of a system for converting a feedstock into a gas, in accordance with an embodiment of the present invention. 5 is a schematic diagram of a system for converting a carbonaceous feed to a gas, in accordance with an embodiment of the present invention. FIG. 6 is a diagram of a system for converting a spent feed to a gas in accordance with an embodiment of the present invention. BRIEF DESCRIPTION OF THE DRAWINGS Figure 7 illustrates various downstream applications of a product provided by a system for converting a carbonaceous feed to a gas in accordance with an embodiment of the present invention. An embodiment of the invention is a variety of downstream applications 148 200817501 of a product provided by a system for converting a carbonaceous feed to a gas. Figure 9 illustrates an embodiment for the use of carbon in accordance with an embodiment of the present invention. Various downstream applications of the products provided by the system for converting feed to gas. Figure 10 depicts various downstream products of a product provided by a system for converting feedstock into gas in accordance with an embodiment of the present invention. Application Figure 11. Figure 11 is a flow chart showing the use of a control system for controlling a vaporization process for converting a carbonaceous feed to a gas in accordance with an embodiment of the present invention. Figure 12 illustrates an embodiment in accordance with the present invention. By way of a schematic diagram of a computing platform, and exemplary components thereof, that can be used to control a vaporization process for converting a carbonaceous feed to a gas. Figure 13 is a diagram showing a central control system in accordance with an embodiment of the present invention. Figure 14 is a schematic illustration of an at least partially dispersed control system in accordance with an embodiment of the present invention. Figure 15 is a diagram showing the sensing and response signals received and transmitted by a control system from a vaporization system, respectively, for controlling one or more processes implemented in the vaporization system, in accordance with an embodiment of the present invention. Figure 16 continues to illustrate various apparatus, modules, and sub-systems for integrating a system control system (for converting a carbonaceous feedstock into a specific composition and various possible downstream applications) in accordance with an embodiment of the present invention. Schematic representation of multiple sensing and response access points for the system. 149 200817501 Figure 17 illustrates a schematic diagram of a conversion system that can be input to a system (converting a carbonaceous feed to a gas) in accordance with an embodiment of the present invention. Figure 18 is a diagram showing an example of the operation performed by the control system of Figure 14. Figure 19 is a schematic illustration of a converter that can convert a carbon-containing feed to a gas, in accordance with an embodiment of the present invention. Figure 20 is a schematic illustration of a converter that can convert a carbon-containing feed to a gas, in accordance with an embodiment of the present invention. Figure 21 is a schematic illustration of a converter that can convert a carbon-containing feed to a gas, in accordance with an embodiment of the present invention. Figure 22 is a schematic illustration of a converter that can convert a carbon-containing feed to a gas, in accordance with an embodiment of the present invention. Figure 23 is a schematic illustration of a converter that can convert a carbon-containing feed to a gas, in accordance with an embodiment of the present invention. Figure 24 is a diagram showing a heat recovery subsystem of a vaporization process that converts a carbon-containing feed into a gas in accordance with an embodiment of the present invention. Figure 25 is a diagram showing a heat recovery subsystem of a vaporization process that converts a carbon-containing feed into a gas in accordance with an embodiment of the present invention. Figure 26 is a diagram showing a heat recovery subsystem of a vaporization process that can convert a carbon-containing feed into a gas according to an embodiment of the present invention. Figure 0 is used to control the control process for the controller to be used for use. A schematic representation of a vaporizer used in a vaporization system controlled by a control system in accordance with the present invention - an embodiment, will be illustrated in the accompanying drawings. Flow chart. Fig. 28 shows the gasification process occurring in the regions 2 and 3 of the vaporizer in Fig. 27. Fig. 29 depicts a schematic flow chart of a cryogenic gasification apparatus incorporating an exemplary gas conditioning system (which incorporates a downstream gas bow engine) in accordance with an embodiment of the present invention. Figure 30 does not illustrate the address layout of the entire gasification system in accordance with an embodiment of the present invention. Figure 31 shows the layout of the storage of urban solid waste Qin. Figure 32 is a perspective view of one embodiment of the vaporizer showing in detail the feed inlet, gas outlet, residue outlet, carrier arm enclosure, and inlet and outlet ports. Figure 33 is a side elevational view of the vaporizer shown in Figure 32, detailing the air boxes, the residue container, and the dust collector. Figure 34 is a central longitudinal section through the vaporizer shown in Figures 32 and 33, showing in detail the feed input, gas discharge, residue discharge, lateral transfer equipment, thermocouple, and inlet and outlet. Figure 35 shows an exploded cross-sectional view showing in detail the bellows, the load-bearing arm fingers, the residue picker bolts, and the serrated edges of the step C. Figure 36 is a cross-sectional view of the vaporizer of Figures 3 and 33 showing the refractory material in detail. Figure 37 shows the bellows assembly of steps A and B of the vaporizer shown in Figures 32 through 36. 151 200817501 Figure 38 shows the steps of the vaporizer shown in Figures 32 to 36 (: a cross-sectional view of the bellows. Figure 39 shows a cross-sectional view of the vaporizer of Figures 32 to 36, showing the bellows in detail. The dust seal of the multi-finger carrying arm of the vaporizer shown in Figs. 32 to 36 is shown in detail. Fig. 41 shows the dust removing system of one embodiment of the vaporizer shown in Figs. 32 to 36, showing in detail Dust pusher, dust can attachment, baffle, operating handle and chain mechanism. Figure 42 shows in detail the ice carrier enclosure of the vaporizer shown in Figures 32 to 36. Fig. 43 is a view showing a position of a level switch according to an embodiment of the present invention. Fig. 44 is a view showing the vaporizer, the gas recombination chamber, and the residue adjustment chamber. Figure 45 is a cross-sectional view showing the structure of the vaporizer, the gas recombination chamber, and the residue adjustment chamber. Fig. 46 is a schematic view of the gas recombination chamber. Fig. 47 is a view of the recombination chamber wall. The figure is a top view of the recombination chamber showing the plasma torches, and The positions of the air and vapor nozzles are shown in Fig. 49. The arrangement of the rotary inlets around the recombination chamber is shown in Fig. 50. Fig. 50 shows the connection of the plasma torches on the recombination chamber. Fig. 51A is a diagram of Fig. 46. A cross-sectional view of the recombination chamber. 152 200817501 Figure 5B is a diagram showing the gas flow in a vaporizer comprising the gas recombination system of the present invention, the gas recombination system containing the recombination chamber of Figure 46. Figure 5C Air is injected from the air inlet into the recombination chamber shown in Fig. 46 and its effect on the internal gas flow. Fig. 52 is a block diagram of the action of the residue adjustment system. Fig. 53 shows the actual operation of the residue adjustment system. The figure and its connection to the vaporizer and the baghouse filter are shown. Fig. 54 is a cross-sectional view showing the residue adjusting chamber. Fig. 55 is another view showing the residue adjusting chamber. 56 shows a view of the residue conditioning chamber and a quenching trough having a conveyor belt for conveying vitrification to a stockpile. Figure 57 shows the entire residue adjustment system from another angle. And also shown for this The support structure of the remainder adjustment chamber. Fig. 58 shows the configuration of the residual gas adjustment system having the residue adjustment chamber. Fig. 59 is a flow chart showing the entire system, and more specifically, the gas adjustment system ( GCS) Figure 60 shows a configuration of a gas conditioning system integrated with a syngas conditioning system in accordance with an embodiment of the present invention. Figure 61 is a detailed illustration of a heat exchanger and is shown for controlling to the heat exchange Air-to-process process air ventilator. Figure 62 shows a dry injection system whereby carbon is held in a storage hopper and supplied to the syngas stream using a rotating screw. The syngas 153 200817501 flow tube is tilted at an angle so that carbon that does not enter the gas stream will roll into the baghouse. Figure 63 shows an illustrative overview of a dry injection system in combination with the filter bag. Figure 64 shows an exemplary schematic of a hydrogen chloride scrubber and associated components. Figure 65 shows a system for collecting and storing waste ice from the gas conditioning system. Figure 66 is a flow chart showing the process of a hydrogen sulfide removal process using a Thiopaq based bioreactor in accordance with one embodiment of the present invention. Figure 67 is a diagram of a gas homogenization system in which a gas system is delivered from a single source to a single homogeneous chamber and then to multiple engines, each having its own gas/liquid separator and Heater. Figure 68 is a high level schematic view of a gasification system and its control system of a certain volume homogenization chamber in accordance with an embodiment of the present invention. • * · Figure 70 is another illustration of the gasification and control system of Figure 69. Figure 71 is a flow chart for controlling the control mechanism of one of the gasification systems of Figures 69 and 70. Figure 72 is a flow diagram of another control mechanism for controlling the gasification system of Figures 69 and 70, wherein the system is more suitable for use in the gasification process to add steam. Figure 73 is a flow diagram of another control mechanism for controlling a vaporization process 154 200817501, in accordance with an embodiment of the present invention. Figure 74 is a flow diagram of another control mechanism for controlling a vaporization process, in accordance with an embodiment of the present invention. Figure 75 is a flow diagram of another control mechanism for controlling a vaporization process in accordance with an embodiment of the invention. [Main component symbol description] 10, 120 Vaporization system 54 Particle and dust removal system 100, 1000 Plasma converter 150 Plasma heat source 202 Inductive component 206 Response component 400 Solid residue regulator 450 Slag treatment heat source 500 Gas-to -air heat exchanger 599 steam generator heat exchanger 600 converter gas regulator 625 alloy 700 homogenization system 800 control system 2200 vaporizer 2202 vaporization chamber 2204 feed inlet 155 200817501 2206 2208 2209 2212 , 2214 , 2216 2220 2222 2228 , 2230, 2232 2240(a) v 2240(b) 2244 2256 2258 2260 2262 2264 22 6 6 2268 2269 2270 2272 , 2274 , 2276 227.8 2280 2282 2302 2304 2308 Gas outlet residue outlet screw conveyor step maintenance access 埠 carrying arm Narrow-shaped track rectangular block electric variable speed motor motor output rod drive chain gear driven chain shaft chain member bracket position sensor hole-shaped floor bellows air input pipe connection flange shield hole-shaped top plate structure support member elastic strip 156 200817501 2310 Dust removal facility 23 12 Metal plate 23 14 Dust outlet 23 16 Blinds 2318 Connection position 2320 Chain 2322 Driven dust extractor 2 3 24 Operating rod 2326 Load arm body 2328 Load arm fingers 2402 High density chrome oxide layer 24 04 High density alumina layer 2406 Outside very low density insulation Plate 3 2 00 Gas Recombination System (GRS) 3202 Cylindrical or tubular recombination chamber 3 204 Outlet inlet 3208, 4230 Plasma torch 3212 Vortex 埠 4200 Residue adjustment system 4203 Vitrified slag 4204 Slag stock 4210 Main conveyor 4220 Residue Adjustment Chamber 4222 Storage Tank 4224 Barrier 157 200817501 4228 Gas Outlet 4240 Quenching Barrel 4250 Residual Gas Regulator 4252 Air to Gas Heat Exchanger 42 54 Bag Filter 4256 Second Heat Exchanger 42 5 8 Activated Carbon Bed 4270, 7232 Support structure 5200 Syngas to air heat exchanger 5202 Tube side 5206 Shell side 5210, 6250 Blower 6200 Gas adjustment system 6210 Evaporative cooler 6220 Dry injection system 62 3 0 Filter bag 6240 Hydrogen chloride scrubber 6252 Gas cooling 6260 carbon filter, bed 6270 hydrogen sulfide removal system System 6272 Brush 6274 Bioreactor 7210 Desuperheater 7220 Gas/Liquid Separator 7230 Syngas Storage Tank 158 200817501 8000 8102 8104, 8106 8112, 8114, 8116 8113, 8120 8115 8122 8124 8126, 8128 8130 8250 '8350 : 8550 8252, 8352, 8552, 8254, 8354, 8554, 8256, 8356, 8556, 8258, 8558, 8658 8260, 8360, 8560, 8262, 8362, 8562, 8264, 8364, 8564, 8266, 8366, 8566, 8268 > 8568 8270, 8370, 8570, 8272:8372 8274, 8374, 8574 Homogeneous Chamber (HC) Control System Indication Control Temperature Sensing 70 Pieces Pressure Sensing Element Variable Frequency Drive and Motor Assembly Pressure Control Valve Control Valve Control Indicator Flow Induction Element Gas Analyzer Converter Solid Height Debt Module Transfer Unit Controller Transfer Unit Total MSW + HCF Feed Rate Syngas (Product Gas) Carbon Content Detection Module MSW : HCF Proportional Controller MSW/HCF Separator MSW Feed Rate HCF Feed Rate syngas fuel value determines module fuel: air ratio controller syngas Test module total air flow controller 159 200817501 8276 , 8376 ' 8566 ' 8676 8278 , 8378 , 8578 , 8678 8280 , 8380 , 8580 , 8680 8282 , 8382 , 8582 , 8682 8284 , 8384 , 8584 , 8684 8367 , 8667 8369 : 8669 8371, 8671 8390, 8690 8392, 8692 8552 8572, 8672 8596 8698 9200 9202 9204 9210 9212 9214 9216 9218 9220 9222 Total air flow process temperature detection module temperature controller air flow distribution plasma thermal synthesis gas [H2] content Determining the module synthesis gas [CO] content determines the module fuel: vapor ratio controller steam flow calculation steam addition rate transfer unit controller synthesis gas flow value determination module total feed controller synthesis gas (product gas) opacity detection Module Initial MSW Processing System MSW Material Pile Road MSW Storage Building Door Net Wall · Channel Loader MS W Grounding System Input Transmitter 160 200817501 9230 Magnetic Separator 9240 Feed Conveyor 9242 In-Transport Input Hopper 9250 Separate System 9260 Gas Engine 9299 Burning Tower i 161

Claims (1)

200817501 X. Patent Application Park: 1 · A control system for controlling a vaporization process that converts a carbonaceous feed into a gas suitable for immediate use in a selected downstream application, the system comprising: a plurality of sensing elements for sensing a characteristic of the gas; one or more computing platforms, the communication link to the one or more sensing elements to access a characteristic value representative of the sensing characteristics; A predetermined range of class values (which defines the characteristics of the gas suitable for use in the selected downstream application) for comparison; and one or more process control parameters are calculated that help maintain the characteristic value at the preset And a plurality of response elements operatively linked to the one or more processing devices and operable to cause the processing to be effective to adjust characteristics of the gas, and the communication link to the one or more calculations Process control parameters and operate the devices based on the parameters. 2. The control system of claim 1 wherein the control system is implemented in a real-time manner to provide an immediate response to the inductive characteristics. 3. The control system of claim i, wherein the one or more induced characteristics comprise one or more of: the gas stream, the pressure of the gas, and a component of the gas 'and wherein the process controls The parameters include one or more input rates of an additive, an input rate of a feed, an air to fuel ratio, a ratio of municipal solid waste (Msw) to high carbon feed (hcf), and a vapor pair. The proportional value of the fuel. 162