Catalyst regeneration energy recovery heat pump system

By optimizing the catalyst regeneration energy recovery heat pump system, the problem of insufficient energy utilization during catalyst regeneration was solved, achieving efficient and economical energy recovery and utilization, and improving the overall energy efficiency of oil refining production.

CN121782768APending Publication Date: 2026-04-03李华玉
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Patent Information

Authority / Receiving Office
CN · China
Patent Type
Applications(China)
Current Assignee / Owner
Filing Date
2025-11-09
Publication Date
2026-04-03

AI Technical Summary

Technical Problem

The existing catalyst regeneration process suffers from irreversible temperature loss, insufficient utilization of flue gas energy, and lack of integration with oil refining processes, resulting in low energy utilization efficiency.

Method used

A series of catalyst regeneration energy recovery heat pump systems were designed. By combining components such as heat source regenerator, compressor, heat exchanger, combustion chamber, and expander, the flue gas energy utilization process is optimized, and fuel passages and auxiliary combustion chambers are added to improve flue gas temperature and energy utilization value.

Benefits of technology

Reduce irreversible temperature loss, improve energy utilization efficiency, enhance the thermal energy grade and refrigeration/heating utilization in the catalyst regeneration process, improve system performance index, and reduce costs.

✦ Generated by Eureka AI based on patent content.

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Abstract

The invention provides a catalyst regeneration energy recovery heat pump system, and belongs to the technical field of heat pumps. An external air channel is communicated with a charring-regeneration system through a heat source regenerator, the charring-regeneration system is further provided with a smoke channel which is communicated with the outside through a heat exchanger and the heat source regenerator, the charring-regeneration system is further provided with a CO-rich smoke channel which is communicated with a combustion chamber through a compressor, and the external air channel is communicated with a second compressor through a regenerator. The second compressor communicates with a combustion chamber through a high-pressure air channel via a heat exchanger, the combustion chamber communicates with an expansion machine through a fuel gas channel, the expansion machine communicates with a second expansion machine through a fuel gas channel via a heat supplier, and the outside communicates with a third compressor through an air channel. The third compressor communicates with a heat regenerator through an air channel and then communicates with a second expansion machine through a low-pressure port, and the second expansion machine communicates with the outside through a gas channel; and the heat supplier is communicated with the outside through a heated medium channel to form a catalyst regeneration energy recovery heat pump system.
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Description

Technical fields:

[0001] This invention belongs to the field of thermodynamics and heat pump technology. Background technology:

[0002] Catalytic cracking is the process of producing light petroleum products such as liquefied petroleum gas, gasoline, and diesel from heavy petroleum hydrocarbons under the action of a catalyst. When feedstock undergoes catalytic cracking on a catalyst, on the one hand, it generates products such as gases, gasoline, and diesel through cracking and other reactions; on the other hand, condensation reactions occur simultaneously to generate coke deposited on the catalyst surface—which reduces the activity of the catalyst.

[0003] Catalyst regeneration involves burning away the coke deposited on the catalyst with air to restore its activity. This process releases a large amount of high-temperature heat energy, which should be fully utilized. Currently, the main method for recovering energy from regenerated flue gas is to install waste heat boilers to generate steam or further generate power. However, careful analysis reveals the following problems:

[0004] (1) There is a large irreversible loss of temperature difference in the coking process; (2) The composition, temperature and quantity of flue gas are not considered at the same time in the utilization stage; (3) The flue gas energy utilization technology needs to be improved. There is a lot of room for improvement in both power utilization and heating utilization; (4) The flue gas energy recovery is not combined with the overall energy use of the oil refining process to enhance its application value.

[0005] Based on the fundamental principles of simplicity, initiative, safety, and efficiency in energy utilization, this invention presents a catalyst regeneration energy recovery heat pump system with a reasonable process and simple structure, which achieves efficient / high-value recovery and utilization of catalyst regeneration energy. Summary of the Invention:

[0006] The main objective of this invention is to provide a catalyst regeneration energy recovery heat pump system. The specific contents of the invention are described in detail below:

[0007] 1. The catalyst regeneration energy recovery heat pump system mainly consists of a heat source regenerator, a coke combustion-regeneration system, a compressor, a second compressor, a heat exchanger, a combustion chamber, an expander, a heater, a second expander, a third compressor, and a regenerator. An external air passage connects to the coke combustion-regeneration system via the heat source regenerator. The coke combustion-regeneration system also has a flue gas passage connecting to the outside via the heat exchanger and the heat source regenerator. The coke combustion-regeneration system also has a CO-rich flue gas passage connecting to the combustion chamber via the compressor. An external air passage connects to the second compressor via the regenerator. The second compressor has a high-efficiency... The compressed air passage is connected to the combustion chamber via a heat exchanger. The combustion chamber also has a gas passage connected to the expander. The expander also has a gas passage connected to the second expander via a heater. An external air passage connects to the third compressor. The third compressor also has an air passage connected to the regenerator and then to the second expander via a low-pressure port. The second expander also has a gas passage connected to the outside. The heater also has a heated medium passage connected to the outside. The expander and the second expander are connected to the compressor, the second compressor, and the third compressor and transmit power, forming a catalyst regeneration energy recovery heat pump system.

[0008] 2. The catalyst regeneration energy recovery heat pump system is the catalyst regeneration energy recovery heat pump system described in item 1, with an external fuel channel connected to the combustion chamber to form the catalyst regeneration energy recovery heat pump system.

[0009] 3. The catalyst regeneration energy recovery heat pump system is an auxiliary combustion chamber added to the catalyst regeneration energy recovery heat pump system described in item 1 or 2. The auxiliary combustion chamber is connected to the external fuel channel. The coke-regeneration system is adjusted so that the flue gas channel is connected to the heat exchanger, and the flue gas channel of the coke-regeneration system is connected to the auxiliary combustion chamber. The auxiliary combustion chamber is then connected to the heat exchanger via a flue gas channel, thus forming the catalyst regeneration energy recovery heat pump system.

[0010] 4. The catalyst regeneration energy recovery heat pump system mainly consists of a heat source regenerator, a coke combustion-regeneration system, a compressor, a second compressor, a heat exchanger, a combustion chamber, an expander, a heater, a second expander, a third compressor, a regenerator, and a flue gas fan. Externally, it has an air passage connecting to the coke combustion-regeneration system via the compressor and the heat source regenerator. The coke combustion-regeneration system also has a flue gas passage connecting to the outside via the flue gas fan, heat exchanger, and heat source regenerator. The coke combustion-regeneration system also has a CO-rich flue gas passage connecting to the combustion chamber. Externally, it has an air passage connecting to the second compressor via the regenerator. The second compressor has a high-pressure air supply... The gas passage is connected to the combustion chamber via a heat exchanger. The combustion chamber also has a gas passage connected to the expander. The expander also has a gas passage connected to the second expander via a heater. Externally, there is an air passage connected to the third compressor. The third compressor also has an air passage connected to the regenerator and then connected to the second expander via a low-pressure port. The second expander also has a gas passage connected to the outside. The heater also has a heated medium passage connected to the outside. The expander and the second expander are connected to the second and third compressors and transmit power. The flue gas fan is connected to the compressor and transmits power, forming a catalyst regeneration energy recovery heat pump system.

[0011] 5. The catalyst regeneration energy recovery heat pump system is the catalyst regeneration energy recovery heat pump system described in item 4, wherein a fuel passage is added to the combustion chamber to connect with the outside, forming a catalyst regeneration energy recovery heat pump device.

[0012] 6. The catalyst regeneration energy recovery heat pump system is an auxiliary combustion chamber added to the catalyst regeneration energy recovery heat pump system described in item 4 or 5. An external fuel channel is connected to the auxiliary combustion chamber. The coke-regeneration system is changed from having a flue gas channel connected to the flue gas fan to having a flue gas channel connected to the auxiliary combustion chamber. The auxiliary combustion chamber is then connected to the flue gas fan via a flue gas channel, thus forming the catalyst regeneration energy recovery heat pump system.

[0013] 7. The catalyst regeneration energy recovery heat pump system is any one of the catalyst regeneration energy recovery heat pump systems described in items 1-6, wherein the external air passage is connected to the second compressor via the regenerator, and then the second compressor has an air passage connected to itself via the regenerator, thereby forming the catalyst regeneration energy recovery heat pump system.

[0014] 8. A catalyst regeneration energy recovery heat pump system is formed by adding a second regenerator to any of the catalyst regeneration energy recovery heat pump systems described in items 1-6. The external air passage connecting the regenerator and the second compressor is adjusted to connect the external air passage connecting the regenerator and the second regenerator to the second compressor. The gas passage connecting the heater to the second expander is adjusted to connect the heater to the second expander via the second regenerator, thus forming a catalyst regeneration energy recovery heat pump system.

[0015] 9. A catalyst regeneration energy recovery heat pump system is any one of the catalyst regeneration energy recovery heat pump systems described in items 1-6, with the addition of a second regenerator. The external air passage is adjusted to connect the second compressor via the regenerator, and then the second compressor has an air passage connecting it to the regenerator and the second regenerator. The gas supply passage is adjusted to connect the second expander via the second regenerator, thus forming a catalyst regeneration energy recovery heat pump system.

[0016] 10. A catalyst regeneration energy recovery heat pump system is any one of the catalyst regeneration energy recovery heat pump systems described in items 1-6, with the addition of a second regenerator. The external air passage connecting the regenerator and the second compressor is adjusted to connect the external air passage connecting the regenerator and the second regenerator to the second compressor. The gas passage connecting the heater to the second expander is adjusted to connect the heater to the second expander, and then the second expander has a gas passage connecting to itself via the second regenerator, thus forming a catalyst regeneration energy recovery heat pump system.

[0017] 11. A catalyst regeneration energy recovery heat pump system is any one of the catalyst regeneration energy recovery heat pump systems described in items 1-6, with the addition of a second regenerator. The external air passage is adjusted to connect the second compressor via the regenerator, and then the second compressor has an air passage connected to itself via the second regenerator. The heater is adjusted to connect the second expander via a gas passage, and then the second expander has a gas passage connected to itself via the second regenerator, thus forming a catalyst regeneration energy recovery heat pump system. Attached image description:

[0018] Figure 1 This is a principle thermodynamic system diagram of a catalyst regeneration energy recovery heat pump system provided by the present invention.

[0019] Figure 2 This is a second principle thermodynamic system diagram of a catalyst regeneration energy recovery heat pump system provided by the present invention.

[0020] Figure 3 This is a third principle thermodynamic system diagram of a catalyst regeneration energy recovery heat pump system provided by the present invention.

[0021] Figure 4 This is a fourth principle thermodynamic system diagram of a catalyst regeneration energy recovery heat pump system provided by the present invention.

[0022] Figure 5This is the fifth principle thermodynamic system diagram of the catalyst regeneration energy recovery heat pump system provided by the present invention.

[0023] Figure 6 This is the sixth principle thermodynamic system diagram of the catalyst regeneration energy recovery heat pump system provided by the present invention.

[0024] Figure 7 This is the seventh principle thermodynamic system diagram of the catalyst regeneration energy recovery heat pump system provided by the present invention.

[0025] Figure 8 This is the eighth principle thermodynamic system diagram of the catalyst regeneration energy recovery heat pump system provided by the present invention.

[0026] Figure 9 This is the ninth principle thermodynamic system diagram of the catalyst regeneration energy recovery heat pump system provided by the present invention.

[0027] Figure 10 This is the tenth principle thermodynamic system diagram of the catalyst regeneration energy recovery heat pump system provided by the present invention. Figure 11 This is the 11th principle thermodynamic system diagram of the catalyst regeneration energy recovery heat pump system provided by the present invention.

[0028] In the diagram, 1-heat source regenerator, 2-coke burning-regeneration system, 3-compressor, 4-second compressor, 5-heat exchanger, 6-combustion chamber, 7-expander, 8-heater, 9-second expander, 10-third compressor, 11-regenerator, 12-auxiliary combustion chamber, 13-smoke machine, 14-second regenerator; among them, the separation and purification components required for the coke burning-regeneration system are considered as part of the coke burning-regeneration system and are not listed separately. Detailed implementation method:

[0029] First, it should be noted that the structure and process are not repeated unless necessary, and obvious processes are not described. The invention will now be described in detail with reference to the accompanying drawings and examples.

[0030] Figure 1 The catalyst regeneration energy recovery heat pump system shown is implemented as follows:

[0031] (1) Structurally, it mainly consists of a heat source regenerator, a coke-regeneration system, a compressor, a second compressor, a heat exchanger, a combustion chamber, an expander, a heater, a second expander, a third compressor, and a regenerator; an external air passage connects to the coke-regeneration system 2 via the heat source regenerator 1, the coke-regeneration system 2 also has a flue gas passage connecting to the outside via the heat exchanger 5 and the heat source regenerator 1, the coke-regeneration system 2 also has a CO-rich flue gas passage connecting to the combustion chamber 6 via the compressor 3, an external air passage connects to the second compressor 4 via the regenerator 11, and the second compressor 4 has a high-pressure An air passage connects to a combustion chamber 6 via a heat exchanger 5. The combustion chamber 6 also has a gas passage connecting to an expander 7. The expander 7 also has a gas passage connecting to a second expander 9 via a heater 8. An external air passage connects to a third compressor 10. The third compressor 10 also has an air passage connecting to a regenerator 11, and then connects to the second expander 9 via a low-pressure port. The second expander 9 also has a gas passage connecting to the outside. The heater 8 also has a heated medium passage connecting to the outside. The expander 7 and the second expander 9 connect to the compressor 3, the second compressor 4, and the third compressor 10 and transmit power.

[0032] (2) In terms of process, external air flows through the heat source regenerator 1 to absorb heat and increase its temperature, and then enters the coke-regeneration system 2 to participate in combustion; air and catalyst coke coking and undergo a series of processes including combustion to achieve catalyst regeneration; the coke-regeneration system 2 discharges flue gas with different CO contents in two separate paths; the flue gas discharged from the coke-regeneration system 2 (with low or no CO content) is separated and purified and then supplied to the heat exchanger 5; the flue gas flows through the heat exchanger 5 and the heat source regenerator 1 to gradually release heat and decrease its temperature before being discharged to the outside; the CO-rich flue gas discharged from the coke-regeneration system 2 is separated and purified and then flows through the compressor 3 to increase its pressure and temperature, and then is supplied to the combustion chamber 6; external air flows through the regenerator 11 to absorb heat and increase its temperature, flows through the second compressor 4 to increase its pressure and temperature, flows through the heat exchanger 5 to absorb heat and increase its temperature, and then enters the combustion chamber 6 to participate in combustion; the CO-rich flue gas and compressed air are burned in the combustion chamber 6 to form high-temperature gas, the high-temperature gas flows through the expander 7 to decrease its pressure and do work, and flows through the heater 8 to release heat and decrease its temperature. The air flows through the second expander 9 to reduce pressure and perform work, and then is discharged to the outside. The outside air flows through the third compressor 10 to increase pressure and temperature, flows through the regenerator 11 to release heat and cool down, and enters the second expander 9 through the intermediate low-pressure port to reduce pressure and perform work, and then is discharged to the outside. The flue gas and CO-rich flue gas emitted by the coke-regeneration system 2 provide driving heat load. The air and flue gas carry away the low-temperature emission heat load through the heat source process. The air and gas provide low-temperature heat load through the heat pump process. The heated medium obtains medium-temperature heat load through the heater 8. The mechanical energy output by the expander 7 and the second expander 9 provides power to the compressor 3, the second compressor 4 and the third compressor 10, or the mechanical energy output by the expander 7 and the second expander 9 provides power to the compressor 3, the second compressor 4 and the third compressor 10 and the outside, or the expander 7, the second expander 9 and the outside jointly provide power to the compressor 3, the second compressor 4 and the third compressor 10, forming a catalyst regeneration energy recovery heat pump system.

[0033] Figure 2 The catalyst regeneration energy recovery heat pump system shown is implemented as follows:

[0034] exist Figure 1 In the catalyst regeneration energy recovery heat pump system shown, an external fuel channel is added and connected to the combustion chamber 6. Fuel, CO-rich flue gas and compressed air are burned in the combustion chamber 6 to produce high-temperature gas. The high-temperature gas flows through the expander 7 to reduce pressure and do work, and then is supplied to the heater 8. The added fuel provides driving heat load through the combustion chamber 6, forming a catalyst regeneration energy recovery heat pump system.

[0035] Figure 3 The catalyst regeneration energy recovery heat pump system shown is implemented as follows:

[0036] (1) Structurally, in Figure 2In the catalyst regeneration energy recovery heat pump system shown, an auxiliary combustion chamber 12 is added, and an external fuel channel is connected to the auxiliary combustion chamber 12. The coke-regeneration system 2, which was previously connected to the heat exchanger 5 via a flue gas channel, is now connected to the auxiliary combustion chamber 12 via a flue gas channel. The auxiliary combustion chamber 12 is then connected to the heat exchanger 5 via a flue gas channel.

[0037] (2) In terms of process, with Figure 2 Compared to the catalyst regeneration energy recovery heat pump system shown, the difference is that: external fuel enters the auxiliary combustion chamber 12, and the flue gas emitted by the coke-regeneration system 2 enters the auxiliary combustion chamber 12. The fuel and flue gas are burned in the auxiliary combustion chamber 12 to form flue gas at a higher temperature, which is then supplied to the heat exchanger 5. The increased fuel provides the driving heat load through the auxiliary combustion chamber 12, forming the catalyst regeneration energy recovery heat pump system.

[0038] Figure 4 The catalyst regeneration energy recovery heat pump system shown is implemented as follows:

[0039] (1) Structurally, it mainly consists of a heat source regenerator, a coke-regeneration system, a compressor, a second compressor, a heat exchanger, a combustion chamber, an expander, a heater, a second expander, a third compressor, a regenerator, and a flue gas fan; externally, there is an air passage that connects to the coke-regeneration system 2 via the compressor 3 and the heat source regenerator 1. The coke-regeneration system 2 also has a flue gas passage that connects to the outside via the flue gas fan 13, the heat exchanger 5, and the heat source regenerator 1. The coke-regeneration system 2 also has a CO-rich flue gas passage that connects to the combustion chamber 6. Externally, there is an air passage that connects to the second compressor 4 via the regenerator 11. The second compressor 4 has high-pressure air. The channel is connected to the combustion chamber 6 via the heat exchanger 5. The combustion chamber 6 also has a gas passage connected to the expander 7. The expander 7 also has a gas passage connected to the second expander 9 via the heater 8. It has an external air passage connected to the third compressor 10. The third compressor 10 also has an air passage connected to the regenerator 11 and then connected to the second expander 9 via a low-pressure port. The second expander 9 also has a gas passage connected to the outside. The heater 8 also has a heated medium passage connected to the outside. The expander 7 and the second expander 9 are connected to the second compressor 4 and the third compressor 10 and transmit power. The smoke hood 13 is connected to the compressor 3 and transmits power.

[0040] (2) In terms of process, with Figure 1Compared to the catalyst regeneration energy recovery heat pump system shown, the difference lies in the following: external air flows through compressor 3 to increase its pressure and temperature, then flows through heat source regenerator 1 to absorb heat and increase its temperature, and then enters coke burning-regeneration system 2 to participate in combustion; air and catalyst coke undergo a series of processes including combustion to achieve catalyst regeneration; coke burning-regeneration system 2 emits flue gas with different CO contents in two separate paths; the flue gas emitted by coke burning-regeneration system 2 (with low or no CO content) is separated and purified, then flows through flue gas fan 13 to reduce pressure and perform work, and then is supplied to heat exchanger 5 for coke burning-regeneration. The CO-rich flue gas emitted by system 2 enters combustion chamber 6 after separation and purification. The mechanical energy output by expander 7, second expander 9 and flue gas fan 13 provides power to compressor 3, second compressor 4 and third compressor 10, or the mechanical energy output by expander 7, second expander 9 and flue gas fan 13 provides power to compressor 3, second compressor 4, third compressor 10 and external components, or expander 7, second expander 9, flue gas fan 13 and external components jointly provide power to compressor 3, second compressor 4 and third compressor 10, forming a catalyst regeneration energy recovery heat pump system.

[0041] Figure 5 The catalyst regeneration energy recovery heat pump system shown is implemented as follows:

[0042] exist Figure 4 In the catalyst regeneration energy recovery heat pump system shown, the combustion chamber 6 is equipped with a fuel passage that connects to the outside. Fuel, CO-rich flue gas and compressed air are burned in the combustion chamber 6 to produce high-temperature gas. The high-temperature gas flows through the expander 7 to reduce pressure and do work, and then is supplied to the heater 8. The increased fuel provides the driving heat load through the combustion chamber 6, forming the catalyst regeneration energy recovery heat pump system.

[0043] Figure 6 The catalyst regeneration energy recovery heat pump system shown is implemented as follows:

[0044] (1) Structurally, in Figure 5 In the catalyst regeneration energy recovery heat pump system shown, an auxiliary combustion chamber 12 is added, and an external fuel channel is connected to the auxiliary combustion chamber 12. The coke-regeneration system 2, which was previously connected to the flue gas machine 13, is now connected to the auxiliary combustion chamber 12, and the auxiliary combustion chamber 12 is further connected to the flue gas machine 13 via a flue gas channel.

[0045] (2) In terms of process, with Figure 5Compared to the catalyst regeneration energy recovery heat pump system shown, the difference is that: external fuel enters the auxiliary combustion chamber 12, and the flue gas emitted by the coke-regeneration system 2 enters the auxiliary combustion chamber 12. The fuel and flue gas are burned in the auxiliary combustion chamber 12 to form flue gas at a higher temperature, which then enters the flue gas fan 13 to reduce pressure and perform work. The increased fuel provides driving heat load through the auxiliary combustion chamber 12, forming the catalyst regeneration energy recovery heat pump system.

[0046] Figure 7 The catalyst regeneration energy recovery heat pump system shown is implemented as follows:

[0047] (1) Structurally, in Figure 1 In the catalyst regeneration energy recovery heat pump system shown, after adjusting the external air channel to connect the second compressor 4 through the regenerator 11 to the external air channel to connect the second compressor 4, the second compressor 4 then has an air channel to connect to itself through the regenerator 11.

[0048] (2) In terms of process, with Figure 1 Compared to the catalyst regeneration energy recovery heat pump system shown, the difference is that: external air enters the second compressor 4 to be pressurized and heated, and after reaching a certain level, it flows through the regenerator 11 to absorb heat and be heated, and then enters the second compressor 4 to continue to be pressurized and heated, thus forming the catalyst regeneration energy recovery heat pump system.

[0049] Figure 8 The catalyst regeneration energy recovery heat pump system shown is implemented as follows:

[0050] (1) Structurally, in Figure 1 In the catalyst regeneration energy recovery heat pump system shown, a second regenerator 14 is added. The external air passage connecting the regenerator 11 and the second compressor 4 is adjusted to connect the external air passage connecting the regenerator 11 and the second regenerator 14 to the second compressor 4. The gas passage connecting the heater 8 to the second expander 9 is adjusted to connect the heater 8 to the second expander 9 via the second regenerator 14.

[0051] (2) In terms of process, with Figure 1 Compared to the catalyst regeneration energy recovery heat pump system shown, the difference is that: the external air flows through the regenerator 11 and the second regenerator 14 to gradually absorb heat and increase temperature, and then enters the second compressor 4 to increase pressure and temperature; the gas discharged from the expander 7 flows through the heater 8 and the second regenerator 14 to gradually release heat and decrease temperature, flows through the second expander 9 to decrease pressure and do work, and then is discharged to the outside, forming a catalyst regeneration energy recovery heat pump system.

[0052] Figure 9 The catalyst regeneration energy recovery heat pump system shown is implemented as follows:

[0053] (1) Structurally, in Figure 1 In the catalyst regeneration energy recovery heat pump system shown, a second regenerator 14 is added. The external air passage is connected to the second compressor 4 through the regenerator 11, and then the second compressor 4 is connected to itself through the regenerator 11 and the second regenerator 14. The gas passage of the heater 8 is connected to the second expander 9, and then the gas passage of the heater 8 is connected to the second expander 9 through the second regenerator 14.

[0054] (2) In terms of process, with Figure 1 Compared to the catalyst regeneration energy recovery heat pump system shown, the difference is that: external air enters the second compressor 4 and is pressurized and heated. After reaching a certain level, it flows through the regenerator 11 and the second regenerator 14 to gradually absorb heat and heat up. Then it enters the second compressor 4 to continue to pressurize and heat up. The gas discharged from the expander 7 flows through the heater 8 and the second regenerator 14 to gradually release heat and cool down. It flows through the second expander 9 to reduce pressure and do work, and then is discharged to the outside, forming the catalyst regeneration energy recovery heat pump system.

[0055] Figure 10 The catalyst regeneration energy recovery heat pump system shown is implemented as follows:

[0056] (1) Structurally, in Figure 1 In the catalyst regeneration energy recovery heat pump system shown, a second regenerator 14 is added. The external air passage is connected to the second compressor 4 through the regenerator 11 and the second regenerator 14, and the external air passage is connected to the second compressor 4 through the regenerator 11 and the second regenerator 14. The gas passage of the heater 8 is connected to the second expander 9, and the heater 8 is connected to the second expander 9. Then the second expander 9 has a gas passage connected to itself through the second regenerator 14.

[0057] (2) In terms of process, with Figure 1 Compared to the catalyst regeneration energy recovery heat pump system shown, the difference is that: external air flows through the regenerator 11 and the second regenerator 14 to gradually absorb heat and increase temperature, and then enters the second compressor 4 to increase pressure and temperature; the gas discharged from the heater 8 enters the second expander 9 to reduce pressure and do work, and after reaching a certain level, it flows through the second regenerator 14 to release heat and decrease temperature, and then enters the second expander 9 to continue to reduce pressure and do work, and then is discharged to the outside, forming a catalyst regeneration energy recovery heat pump system.

[0058] Figure 11 The catalyst regeneration energy recovery heat pump system shown is implemented as follows:

[0059] (1) Structurally, in Figure 1In the catalyst regeneration energy recovery heat pump system shown, a second regenerator 14 is added. The external air passage is connected to the second compressor 4 through the regenerator 11, and then the second compressor 4 is connected to itself through the second regenerator 14. The gas passage of the heater 8 is connected to the second expander 9, and then the second expander 9 is connected to itself through the second regenerator 14.

[0060] (2) In terms of process, with Figure 1 Compared to the catalyst regeneration energy recovery heat pump system shown, the difference lies in the following: external air flows through the regenerator 11 to absorb heat and increase its temperature, and then supplies it to the second compressor 4; the air enters the second compressor 4 to increase its pressure and temperature, and after reaching a certain level, it flows through the second regenerator 14 to absorb heat and increase its temperature, and then enters the second compressor 4 again to continue to increase its pressure and temperature; the gas discharged from the heater 8 enters the second expander 9 to reduce its pressure and do work, and after reaching a certain level, it flows through the second regenerator 14 to release heat and decrease its temperature, and enters the second expander 9 again to continue to reduce its pressure and do work, and then is discharged to the outside, forming the catalyst regeneration energy recovery heat pump system.

[0061] The effects achievable by this invention—the catalyst regeneration energy recovery heat pump system proposed in this invention has the following effects and advantages:

[0062] (1) Technical measures were proposed to improve the thermal energy grade of the catalyst regeneration process and to utilize it for refrigeration / heating.

[0063] (2) Reduce irreversible temperature loss during catalyst regeneration and increase the temperature of the initial driving heat source.

[0064] (3) The variable temperature obtains the driving heat load, thereby improving the performance index of the gas heat pump system by increasing the heat absorption temperature.

[0065] (4) The driving heat load provided by the regenerated flue gas and the regenerated CO-rich flue gas is used in stages to reduce the systemic irreversible loss and improve the energy utilization level of catalyst regeneration.

[0066] (5) Fuel (e.g., refinery gas or purchased fuel) provides high-temperature driving heat load through the combustion chamber, which greatly enhances the cooling / heating value of regenerated flue gas energy.

[0067] (6) Achieve efficient / high-value utilization of flue gas energy with relatively simple technical measures, reduce costs, and improve economic efficiency.

[0068] (7) The heat recovery measures increase the average temperature of the heat pump system during the heat absorption process and decrease the average temperature of the heat pump system during the heat release process. The systemic temperature difference loss is small, which improves the performance index of the device.

[0069] (8) Provides multiple technical solutions, which are conducive to the catalyst regeneration energy recovery heat pump system to better enhance the energy application value.

Claims

1. The catalyst regeneration energy recovery heat pump system mainly consists of a heat source regenerator, a coke-regeneration system, a compressor, a second compressor, a heat exchanger, a combustion chamber, an expander, a heater, a second expander, a third compressor, and a regenerator; an external air passage connects to the coke-regeneration system (2) via the heat source regenerator (1), the coke-regeneration system (2) also has a flue gas passage connecting to the outside via the heat exchanger (5) and the heat source regenerator (1), the coke-regeneration system (2) also has a CO-rich flue gas passage connecting to the combustion chamber (6) via the compressor (3), an external air passage connects to the second compressor (4) via the regenerator (11), and the second compressor (4) has a high-pressure air passage connecting to the heat exchanger (5) via the heat source regenerator (11). The expansion chamber (7) is connected to the combustion chamber (6), and the combustion chamber (6) is also connected to the expander (7) via a gas passage. The expander (7) is also connected to the second expander (9) via a gas passage through the heater (8). The external air passage is connected to the third compressor (10). The third compressor (10) is also connected to the regenerator (11) via an air passage and then connected to the second expander (9) via a low-pressure port. The second expander (9) is also connected to the external air passage. The heater (8) is also connected to the external air passage for the heated medium. The expander (7) and the second expander (9) are connected to the compressor (3), the second compressor (4) and the third compressor (10) and transmit power to form a catalyst regeneration energy recovery heat pump system.

2. The catalyst regeneration energy recovery heat pump system is a catalyst regeneration energy recovery heat pump system according to claim 1, wherein an external fuel channel is added to connect with the combustion chamber (6) to form the catalyst regeneration energy recovery heat pump system.

3. The catalyst regeneration energy recovery heat pump system is an auxiliary combustion chamber (12) added to the catalyst regeneration energy recovery heat pump system described in claim 1 or claim 2. The auxiliary combustion chamber (12) is connected to the external fuel channel. The coke-regeneration system (2) is adjusted to have a flue gas channel connected to the heat exchanger (5) so that the coke-regeneration system (2) has a flue gas channel connected to the auxiliary combustion chamber (12). The auxiliary combustion chamber (12) is then connected to the heat exchanger (5) through a flue gas channel, thus forming the catalyst regeneration energy recovery heat pump system.

4. The catalyst regeneration energy recovery heat pump system mainly consists of a heat source regenerator, a coke-regeneration system, a compressor, a second compressor, a heat exchanger, a combustion chamber, an expander, a heater, a second expander, a third compressor, a regenerator, and a flue gas fan; an external air passage connects to the coke-regeneration system (2) via the compressor (3) and the heat source regenerator (1), the coke-regeneration system (2) also has a flue gas passage connecting to the outside via the flue gas fan (13), the heat exchanger (5), and the heat source regenerator (1), the coke-regeneration system (2) also has a CO-rich flue gas passage connecting to the combustion chamber (6), an external air passage connects to the second compressor (4) via the regenerator (11), the second compressor (4) has a high-pressure air passage connecting to the combustion chamber (6) via the heat exchanger (5), and an external air passage connects to the second compressor (4) via the regenerator (11). The combustion chamber (6) is connected, and the combustion chamber (6) also has a gas passage connected to the expander (7). The expander (7) also has a gas passage connected to the second expander (9) via the heater (8). There is an external air passage connected to the third compressor (10). The third compressor (10) also has an air passage connected to the regenerator (11) and then connected to the second expander (9) via a low-pressure port. The second expander (9) also has a gas passage connected to the outside. The heater (8) also has a heated medium passage connected to the outside. The expander (7) and the second expander (9) are connected to the second compressor (4) and the third compressor (10) and transmit power. The smoke machine (13) is connected to the compressor (3) and transmits power, forming a catalyst regeneration energy recovery heat pump system.

5. The catalyst regeneration energy recovery heat pump system is a catalyst regeneration energy recovery heat pump system as described in claim 4, wherein a fuel channel is added to the combustion chamber (6) to connect with the outside, forming a catalyst regeneration energy recovery heat pump device.

6. The catalyst regeneration energy recovery heat pump system is an auxiliary combustion chamber (12) added to the catalyst regeneration energy recovery heat pump system described in claim 4 or claim 5. The auxiliary combustion chamber (12) is connected to the external fuel channel. The coke-regeneration system (2) is changed from having a flue gas channel connected to the smoke machine (13) to having a flue gas channel connected to the auxiliary combustion chamber (12). The auxiliary combustion chamber (12) is then connected to the smoke machine (13) via a flue gas channel, thus forming the catalyst regeneration energy recovery heat pump system.

7. A catalyst regeneration energy recovery heat pump system is a catalyst regeneration energy recovery heat pump system according to any one of the catalyst regeneration energy recovery heat pump systems described in claims 1-6, wherein the external air channel is connected to the second compressor (4) through the regenerator (11) and then the second compressor (4) is connected to itself through the regenerator (11) after the external air channel is connected to the second compressor (4), thereby forming a catalyst regeneration energy recovery heat pump system.

8. A catalyst regeneration energy recovery heat pump system is a catalyst regeneration energy recovery heat pump system according to any one of claims 1-6, wherein a second regenerator (14) is added, and the external air passage is connected to the second compressor (4) through the regenerator (11) and the second regenerator (14) are connected to the second compressor (4), and the gas passage of the heater (8) is connected to the second expander (9) through the second regenerator (14) and the second expander (9), thereby forming a catalyst regeneration energy recovery heat pump system.

9. A catalyst regeneration energy recovery heat pump system is a catalyst regeneration energy recovery heat pump system according to any one of claims 1-6, wherein a second regenerator (14) is added, and the external air passage is connected to the second compressor (4) through the regenerator (11) and then the second compressor (4) is connected to itself through the regenerator (11) and the second regenerator (14). The gas passage of the heater (8) is connected to the second expander (9) and then the gas passage of the heater (8) is connected to the second expander (9) through the second regenerator (14), thus forming a catalyst regeneration energy recovery heat pump system.

10. A catalyst regeneration energy recovery heat pump system is a catalyst regeneration energy recovery heat pump system according to any one of claims 1-6, wherein a second regenerator (14) is added, and the external air passage is connected to the second compressor (4) through the regenerator (11) and the second regenerator (14) are connected to the second compressor (4), and the gas passage of the heater (8) is connected to the second expander (9) is adjusted so that the heater (8) has a gas passage connected to the second expander (9), and the second expander (9) has a gas passage connected to itself through the second regenerator (14), thereby forming a catalyst regeneration energy recovery heat pump system.

11. A catalyst regeneration energy recovery heat pump system is a catalyst regeneration energy recovery heat pump system according to any one of claims 1-6, wherein a second regenerator (14) is added, and the external air passage is connected to the second compressor (4) through the regenerator (11) and then the second compressor (4) is connected to itself through the second regenerator (14) through the regenerator (11), and the gas passage of the heater (8) is connected to the second expander (9) and then the second expander (9) is connected to itself through the second regenerator (14) through the gas passage, thereby forming a catalyst regeneration energy recovery heat pump system.