Catalyst regeneration energy recovery heat pump system

Abstract

The invention provides a catalyst regeneration energy recovery heat pump system, and belongs to the technical field of heat pumps. An air channel outside is communicated with the charring-regeneration system through a heat source regenerator, the charring-regeneration system is communicated with the outside through a flue gas channel via a heat exchanger and the heat source regenerator, the charring-regeneration system is communicated with the combustion chamber through a CO-rich flue gas channel, and the combustion chamber is communicated with the outside through a flue gas channel via the heat exchanger and the heat source regenerator. The second expansion machine communicates with the heat regenerator through the low-temperature heat medium channel and then communicates with the compressor through a middle port, and the compressor further communicates with the expansion machine through the low-temperature heat medium channel, the heat exchanger and the combustion chamber. The expansion machine is divided into two paths after being communicated with a heat supplier, the first path is communicated with a second expansion machine, the second path is communicated with a heat regenerator, and the heat regenerator is communicated with the outside through a low-temperature heat medium channel via a third expansion machine; and the heat supplier is communicated with the outside through a heated medium channel to form a catalyst regeneration energy recovery heat pump system.

Description

TECHNICAL FIELD

[0001] The present application belongs to the field of thermodynamics and heat pump technology. BACKGROUND

[0002] Catalytic cracking is a process of producing liquefied gas, gasoline and diesel oil and other light oil products from heavy petroleum hydrocarbons under the action of catalysts. When the raw oil is catalytically cracked on the catalyst, on the one hand, gas, gasoline, diesel oil and other products are generated through cracking and other reactions, and on the other hand, a condensation reaction occurs to generate coke deposited on the surface of the catalyst, which reduces the activity of the catalyst.

[0003] People use air to burn off the coke deposited on the catalyst to restore the activity of the catalyst - catalyst regeneration, which releases a large amount of heat energy at a high temperature, which should be fully utilized; the main means of recovering and regenerating flue gas energy today is to set up a waste heat boiler to generate steam, or further to generate power. However, through careful analysis, the following problems are found:

[0004] (1) There is a large irreversible loss of temperature difference in the coke burning process; (2) In the utilization link, the composition, temperature and quantity of the flue gas are not considered simultaneously; (3) The flue gas energy utilization technology needs to be improved, whether it is power utilization or heat utilization, there is a large room for improvement; (4) The flue gas energy recovery is not combined with the overall energy use of the refining production process to improve its application value.

[0005] In line with the basic principles of simple, active, safe and efficient energy utilization, the present application provides a catalyst regeneration energy recovery heat pump system with reasonable process and simple structure, which realizes efficient / high-value recovery and utilization of catalyst regeneration energy. SUMMARY

[0006] The main purpose of the present application is to provide a catalyst regeneration energy recovery heat pump system, and the specific invention contents are described as follows:

[0007] 1. A catalyst regeneration energy recovery heat pump system, mainly composed of a heat source regenerator, a coke-burning and regeneration system, a compressor, a heat exchanger, a combustion chamber, an expander, a heat supplier, a second expander, a regenerator and a third expander; externally, an air passage is connected with the coke-burning and regeneration system through the heat source regenerator, the coke-burning and regeneration system has a flue gas passage connected with the outside through the heat exchanger and the heat source regenerator, the coke-burning and regeneration system has a CO-rich flue gas passage connected with the combustion chamber, the combustion chamber has a flue gas passage connected with the outside through the heat exchanger and the heat source regenerator, the outside has a low-temperature heat medium passage connected with the compressor, the second expander has a low-temperature heat medium passage connected with the regenerator through an intermediate port and connected with the compressor, the compressor has a low-temperature heat medium passage connected with the expander through the heat exchanger and the combustion chamber, the expander has a low-temperature heat medium passage connected with the heat supplier and divided into two paths, the first path connected with the second expander and the second path connected with the regenerator, the regenerator has a low-temperature heat medium passage connected with the outside through the third expander; the heat supplier has a heated medium passage connected with the outside, the expander, the second expander and the third expander are connected with the compressor and transmit power, forming the catalyst regeneration energy recovery heat pump system.

[0008] 2. The catalyst regeneration energy recovery heat pump system of claim 1, externally adding a fuel passage connected with the combustion chamber, forming the catalyst regeneration energy recovery heat pump system.

[0009] 3. The catalyst regeneration energy recovery heat pump system of claim 1 or 2, adjusting the heat source regenerator having an air passage connected with the coke-burning and regeneration system to the heat source regenerator having an air passage divided into two paths, the first path connected with the coke-burning and regeneration system and the second path connected with the combustion chamber, forming the catalyst regeneration energy recovery heat pump system.

[0010] 4. The catalyst regeneration energy recovery heat pump system of any one of claims 1-3, adding an auxiliary combustion chamber, externally having a fuel passage connected with the auxiliary combustion chamber, adjusting the coke-burning and regeneration system having a flue gas passage connected with the heat exchanger to the coke-burning and regeneration system having a flue gas passage connected with the auxiliary combustion chamber, the auxiliary combustion chamber further having a flue gas passage connected with the heat exchanger, forming the catalyst regeneration energy recovery heat pump system.

[0011] 5. The catalyst regeneration energy recovery heat pump system is mainly composed of heat source regenerator, coke burning-regeneration system, compressor, heat exchanger, combustion chamber, expander, heat supplier, second expander, regenerator, third expander, air compressor, smoke machine and second smoke machine. The external air channel is connected with the coke burning-regeneration system through the air compressor and the heat source regenerator. The coke burning-regeneration system has a flue gas channel connected with the external environment through the smoke machine, the heat exchanger and the heat source regenerator. The coke burning-regeneration system has a CO-rich flue gas channel connected with the combustion chamber through the second smoke machine. The combustion chamber has a flue gas channel connected with the external environment through the heat exchanger and the heat source regenerator. The external low-temperature heat medium channel is connected with the compressor. The second expander has a low-temperature heat medium channel connected with the regenerator through the intermediate port and the compressor. The compressor has a low-temperature heat medium channel connected with the expander through the heat exchanger and the combustion chamber. The expander has a low-temperature heat medium channel connected with the heat supplier, which is divided into two paths, the first path is connected with the second expander and the second path is connected with the regenerator. The regenerator has a low-temperature heat medium channel connected with the external environment through the third expander. The heat supplier has a heated medium channel connected with the external environment. The expander, the second expander and the third expander are connected with the compressor and transmit power. The smoke machine and the second smoke machine are connected with the air compressor and transmit power, forming the catalyst regeneration energy recovery heat pump system.

[0012] 6. The catalyst regeneration energy recovery heat pump system is the catalyst regeneration energy recovery heat pump system of the item 5, in which the combustion chamber is additionally provided with a fuel channel connected with the external environment, forming the catalyst regeneration energy recovery heat pump system.

[0013] 7. The catalyst regeneration energy recovery heat pump system is the catalyst regeneration energy recovery heat pump system of the item 5 or 6, in which an auxiliary combustion chamber is additionally provided. The external fuel channel is connected with the auxiliary combustion chamber. The flue gas channel of the coke burning-regeneration system is connected with the smoke machine and is adjusted to be connected with the auxiliary combustion chamber. The auxiliary combustion chamber has a flue gas channel connected with the smoke machine, forming the catalyst regeneration energy recovery heat pump system.

[0014] 8. The catalyst regeneration energy recovery heat pump system is any one of the catalyst regeneration energy recovery heat pump systems of the items 1-7, in which a second regenerator is additionally provided. The external low-temperature heat medium channel is connected with the compressor through the second regenerator. The low-temperature heat medium channel of the regenerator is connected with the external environment through the second regenerator and the third expander, forming the catalyst regeneration energy recovery heat pump system.

[0015] 9. The catalyst regeneration energy recovery heat pump system is any one of the first to the seventh, increase the second regenerator, the low-temperature heat medium channel outside the compressor is adjusted to the low-temperature heat medium channel outside the compressor through the second regenerator, the low-temperature heat medium channel of the regenerator is adjusted to the low-temperature heat medium channel of the regenerator and the third expander, and the low-temperature heat medium channel of the third expander is adjusted to the low-temperature heat medium channel of the third expander and the second regenerator, and the catalyst regeneration energy recovery heat pump system is formed.

[0016] 10. The catalyst regeneration energy recovery heat pump system is any one of the first to the ninth, increase the dehumidification heat exchanger and the gas-liquid separator, the low-temperature heat medium channel of the third expander is adjusted to the low-temperature heat medium channel of the third expander and the dehumidification heat exchanger and the gas-liquid separator, and the low-temperature heat medium channel of the third expander is adjusted to the low-temperature heat medium channel of the third expander and the dehumidification heat exchanger and the gas-liquid separator, and the catalyst regeneration energy recovery heat pump system is formed.

[0017] 11. The catalyst regeneration energy recovery heat pump system is any one of the first to the sixth, increase the dehumidification heat exchanger and the gas-liquid separator, the low-temperature heat medium channel outside the compressor is adjusted to the low-temperature heat medium channel outside the compressor through the dehumidification heat exchanger, and the low-temperature heat medium channel of the third expander is adjusted to the low-temperature heat medium channel of the third expander and the dehumidification heat exchanger and the gas-liquid separator, and the catalyst regeneration energy recovery heat pump system is formed.

[0018] 12. The catalyst regeneration energy recovery heat pump system is any one of the first to the sixth, increase the low-temperature heat exchanger, the air channel outside the compressor is adjusted to the air channel outside the compressor through the low-temperature heat exchanger, the low-temperature heat medium channel of the low-temperature heat exchanger is adjusted to the low-temperature heat medium channel of the low-temperature heat exchanger and the third expander, and the low-temperature heat medium channel of the third expander is adjusted to the air channel of the third expander and the third expander, and the catalyst regeneration energy recovery heat pump system is formed.

[0019] 13. The catalyst regeneration energy recovery heat pump system is any one of the first to the sixth, increase the dehumidification heat exchanger, gas-liquid separator and low temperature heat exchanger, the outside has low temperature heat medium channel and compressor communication adjustment to the outside has air channel through dehumidification heat exchanger and low temperature heat exchanger and compressor communication, the third expander has low temperature heat medium channel and outside communication adjustment to the third expander has air channel through dehumidification heat exchanger and gas-liquid separator and itself communication after the third expander again has air channel and outside communication, gas-liquid separator has condensate pipeline and outside communication, low temperature heat exchanger has low temperature heat medium channel and outside communication, form catalyst regeneration energy recovery heat pump system.

[0020] 14. The catalyst regeneration energy recovery heat pump system is any one of the seventh to the eighth, increase the dehumidification heat exchanger and gas-liquid separator, the outside has low temperature heat medium channel through second regenerator and compressor communication adjustment to the outside has low temperature heat medium channel through dehumidification heat exchanger and second regenerator and compressor communication, the third expander has low temperature heat medium channel and outside communication adjustment to the third expander has low temperature heat medium channel through dehumidification heat exchanger and gas-liquid separator and itself communication after the third expander again has low temperature heat medium channel and outside communication, gas-liquid separator has condensate pipeline and outside communication, form catalyst regeneration energy recovery heat pump system.

[0021] 15. The catalyst regeneration energy recovery heat pump system is any one of the seventh to the eighth, increase the low temperature heat exchanger, the outside has low temperature heat medium channel through second regenerator and compressor communication adjustment to the outside has air channel through low temperature heat exchanger and second regenerator and compressor communication, the third expander has low temperature heat medium channel and outside communication change to the third expander has air channel and outside communication, low temperature heat exchanger has low temperature heat medium channel and outside communication, form catalyst regeneration energy recovery heat pump system.

[0022] 16. The catalyst regeneration energy recovery heat pump system is any one of the seventh to the eighth, increase the dehumidification heat exchanger, gas-liquid separator and low temperature heat exchanger, the outside has low temperature heat medium channel through second regenerator and compressor communication adjustment to the outside has air channel through dehumidification heat exchanger, low temperature heat exchanger and second regenerator and compressor communication, the third expander has low temperature heat medium channel and outside communication adjustment to the third expander has air channel through dehumidification heat exchanger and gas-liquid separator and itself communication after the third expander again has air channel and outside communication, gas-liquid separator has condensate pipeline and outside communication, low temperature heat exchanger has low temperature heat medium channel and outside communication, form catalyst regeneration energy recovery heat pump system.

[0023] 17. The catalyst regeneration energy recovery heat pump system is in any one of the first-16 items described in the catalyst regeneration energy recovery heat pump system, increase the high temperature regenerator, the compressor has low temperature heat medium channel and heat exchanger communication adjustment is compressor has low temperature heat medium channel through high temperature regenerator and heat exchanger communication, the expansion machine has low temperature heat medium channel and heat supply device communication adjustment is expansion machine has low temperature heat medium channel through high temperature regenerator and heat supply device communication, form catalyst regeneration energy recovery heat pump system.

[0024] 18. The catalyst regeneration energy recovery heat pump system is in any one of the first-16 items described in the catalyst regeneration energy recovery heat pump system, increase the high temperature regenerator, the compressor has low temperature heat medium channel and heat exchanger communication adjustment is compressor has low temperature heat medium channel through high temperature regenerator and heat exchanger communication, the expansion machine has low temperature heat medium channel and heat supply device communication adjustment is expansion machine has low temperature heat medium channel through high temperature regenerator and itself communication, the expansion machine has low temperature heat medium channel and heat supply device communication again, form catalyst regeneration energy recovery heat pump system. BRIEF DESCRIPTION OF DRAWINGS

[0025] Figure 1 It is the first kind of principle heat system diagram of catalyst regeneration energy recovery heat pump system provided by the application.

[0026] Figure 2 It is the second kind of principle heat system diagram of catalyst regeneration energy recovery heat pump system provided by the application.

[0027] Figure 3 It is the third kind of principle heat system diagram of catalyst regeneration energy recovery heat pump system provided by the application.

[0028] Figure 4 It is the fourth kind of principle heat system diagram of catalyst regeneration energy recovery heat pump system provided by the application.

[0029] Figure 5 It is the fifth kind of principle heat system diagram of catalyst regeneration energy recovery heat pump system provided by the application.

[0030] Figure 6 It is the sixth kind of principle heat system diagram of catalyst regeneration energy recovery heat pump system provided by the application.

[0031] Figure 7 It is the seventh kind of principle heat system diagram of catalyst regeneration energy recovery heat pump system provided by the application.

[0032] Figure 8 It is the eighth kind of principle heat system diagram of catalyst regeneration energy recovery heat pump system provided by the application.

[0033] Figure 9 is the 9th principle heat system diagram of the catalyst regeneration energy recovery heat pump system according to the present application.

[0034] Figure 10 is the 10th principle heat system diagram of the catalyst regeneration energy recovery heat pump system according to the present application.

[0035] Figure 11 is the 11th principle heat system diagram of the catalyst regeneration energy recovery heat pump system according to the present application.

[0036] Figure 12 is the 12th principle heat system diagram of the catalyst regeneration energy recovery heat pump system according to the present application.

[0037] Figure 13 is the 13th principle heat system diagram of the catalyst regeneration energy recovery heat pump system according to the present application.

[0038] Figure 14 is the 14th principle heat system diagram of the catalyst regeneration energy recovery heat pump system according to the present application.

[0039] Figure 15 is the 15th principle heat system diagram of the catalyst regeneration energy recovery heat pump system according to the present application.

[0040] In the figure, 1 is a heat source regenerator, 2 is a coking-regeneration system, 3 is a compressor, 4 is a heat exchanger, 5 is a combustion chamber, 6 is an expander, 7 is a heat supplier, 8 is a second expander, 9 is a regenerator, 10 is a third expander, 11 is an auxiliary combustion chamber, 12 is an air compressor, 13 is a smoke machine, 14 is a second regenerator, 15 is a second regenerator, 16 is a dehumidification heat exchanger, 17 is a gas-liquid separator, 18 is a low-temperature heat exchanger, and 19 is a high-temperature regenerator. In addition, it should be pointed out that:

[0041] (1) The separation and purification components required by the coking-regeneration system are considered as part of the coking-regeneration system and are not listed separately.

[0042] (2) Taking Figure 12 as an example, Figure 12 the air entering and leaving the heat pump process belongs to the category of low-temperature heat medium; for convenience of expression or to avoid confusion of terms, the air entering and leaving the heat pump process can be replaced by low-temperature heat medium. DETAILED DESCRIPTION

[0043] First of all, it should be pointed out that in the description of structure and process, unnecessary repetition is not performed, and the process that is obvious is not described. The present application will be described in detail below in combination with the drawings and examples.

[0044] Figure 1 The catalyst regeneration energy recovery heat pump system is realized as shown:

[0045] (1) Structurally, it is mainly composed of heat source regenerator, coke burning-regeneration system, compressor, heat exchanger, combustion chamber, expander, heat supplier, second expander, regenerator and third expander; externally, there is an air passage communicating with the coke burning-regeneration system 2 through the heat source regenerator 1, the coke burning-regeneration system 2 also has a flue gas passage communicating with the outside through the heat exchanger 4 and the heat source regenerator 1, the coke burning-regeneration system 2 also has a CO-rich flue gas passage communicating with the combustion chamber 5, the combustion chamber 5 also has a flue gas passage communicating with the outside through the heat exchanger 4 and the heat source regenerator 1, the outside has a low-temperature heat medium passage communicating with the compressor 3, the second expander 8 has a low-temperature heat medium passage communicating with the regenerator 9 after the intermediate port and communicating with the compressor 3, the compressor 3 also has a low-temperature heat medium passage communicating with the expander 6 through the heat exchanger 4 and the combustion chamber 5, the expander 6 also has a low-temperature heat medium passage communicating with the heat supplier 7 and then being divided into two routes-the first route communicating with the second expander 8 and the second route communicating with the regenerator 9, the regenerator 9 also has a low-temperature heat medium passage communicating with the outside through the third expander 10; the heat supplier 7 also has a heated medium passage communicating with the outside, and the expander 6, the second expander 8 and the third expander 10 are connected with the compressor 3 and transmit power.

[0046] (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 4; the flue gas flows through the heat exchanger 4 and the heat source regenerator 1 to gradually release heat and decrease in 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 enters the combustion chamber 5 to burn and generate high-temperature flue gas; the high-temperature flue gas releases heat to the low-temperature heat medium flowing through the combustion chamber 5, and then flows through the heat exchanger 4 and the heat source regenerator 1 to gradually release heat and decrease in temperature before being discharged to the outside; the external low-temperature heat medium enters the compressor 3 to increase pressure and temperature, and the low-temperature heat medium discharged from the regenerator 9 enters the compressor 3 through the intermediate port to increase pressure and temperature; the low-temperature heat medium discharged from the compressor 3 flows through the heat exchanger 4 and the combustion chamber 5 to gradually absorb heat and increase in temperature, and then flows through the heat source regenerator 1 to gradually release heat and decrease in temperature before being discharged to the outside; the external low-temperature heat medium enters the compressor 3 to increase pressure and temperature, and the low-temperature heat medium discharged from the regenerator 9 enters the compressor 3 through the intermediate port to increase pressure and temperature, and the low-temperature heat medium discharged from the compressor 3 flows through the heat exchanger 4 and the combustion chamber 5 to gradually absorb heat and increase in temperature, and then flows through the heat source regenerator 1 to gradually release heat and decrease in temperature before being discharged to the outside; the external low-temperature heat medium enters the compressor 3 to increase pressure and temperature, and the After being depressurized and worked by expander 6, the gas flows through heater 7 to release heat and cool down. It then splits into two streams: the first stream flows through second expander 8 to depressurize and work, then through regenerator 9 to absorb heat and heat up, before entering compressor 3 through the intermediate air inlet port for further pressurization and heating; the second stream enters regenerator 9 to release heat and cool down. The low-temperature heat medium discharged from regenerator 9 flows through third expander 10 to depressurize and work, and is then discharged externally. The flue gas and CO-rich flue gas emitted by coke burning-regeneration system 2 provide the driving heat load, and the air and flue gas carry away the low-temperature emitted heat through the heat source flow process. The load is as follows: the heated medium obtains a medium-temperature heat load through the heater 7, and the low-temperature heat medium provides a low-temperature heat load through the heat pump process; the mechanical energy output by the expander 6, the second expander 8 and the third expander 10 is provided to the compressor 3 as power, or the mechanical energy output by the expander 6, the second expander 8 and the third expander 10 is provided to the compressor 3 and the external environment as power, or the expander 6, the second expander 8, the third expander 10 and the external environment jointly provide power to the compressor 3, forming a catalyst regeneration energy recovery heat pump system.

[0047] Figure 2 The catalyst regeneration energy recovery heat pump system shown is implemented as follows:

[0048] 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 5; fuel and CO-rich flue gas are burned in the combustion chamber 5 to generate high-temperature flue gas, which releases heat to the low-temperature heat medium flowing through the combustion chamber 5, and then provides it to the heat exchanger 4; the added fuel provides high-temperature driving heat load through the combustion chamber 5, forming a catalyst regeneration energy recovery heat pump system.

[0049] Figure 3 The catalyst regeneration energy recovery heat pump system shown is implemented as follows:

[0050] (1) Structurally, inFigure 2 The catalyst regeneration energy recovery heat pump system shown in the figure is different from the catalyst regeneration energy recovery heat pump system shown in the figure in that the heat source regenerator 1 has an air passage connected with the burn-off-regeneration system 2, and the air passage of the heat source regenerator 1 is divided into two paths, the first path is connected with the burn-off-regeneration system 2, and the second path is connected with the combustion chamber 5.

[0051] (2) In terms of process, the catalyst regeneration energy recovery heat pump system shown in the figure is different from the catalyst regeneration energy recovery heat pump system shown in the figure in that the external air passes through the heat source regenerator 1 to absorb heat and rise in temperature, and then is divided into two paths, the first path enters the burn-off-regeneration system 2 to participate in the combustion chamber, and the second path is provided to the combustion chamber 5; the fuel, air and CO-rich flue gas are combusted in the combustion chamber 5 to generate high-temperature flue gas, the high-temperature flue gas releases heat to the low-temperature heat medium flowing through the combustion chamber 5, and then is provided to the heat exchanger 4, forming the catalyst regeneration energy recovery heat pump system. Figure 2

[0052] Figure 4 The catalyst regeneration energy recovery heat pump system shown in the figure is realized in the following way:

[0053] (1) In terms of structure, the catalyst regeneration energy recovery heat pump system shown in the figure is different from the catalyst regeneration energy recovery heat pump system shown in the figure in that an auxiliary combustion chamber 11 is added, the external fuel passage is connected with the auxiliary combustion chamber 11, and the flue gas passage of the burn-off-regeneration system 2 is connected with the auxiliary combustion chamber 11 instead of being connected with the heat exchanger 4, and the auxiliary combustion chamber 11 further has a flue gas passage connected with the heat exchanger 4. Figure 1

[0054] (2) In terms of process, the catalyst regeneration energy recovery heat pump system shown in the figure is different from the catalyst regeneration energy recovery heat pump system shown in the figure in that the external fuel enters the auxiliary combustion chamber 11, the flue gas discharged from the burn-off-regeneration system 2 enters the auxiliary combustion chamber 11, the fuel and the flue gas are combusted in the auxiliary combustion chamber 11 to form flue gas with higher temperature, and then are provided to the heat exchanger 4, forming the catalyst regeneration energy recovery heat pump system. Figure 1

[0055] Figure 5 The catalyst regeneration energy recovery heat pump system shown in the figure is realized in the following way:

[0056] ​​​(1) Structurally, it is mainly composed of heat source regenerator, coke burning-regeneration system, compressor, heat exchanger, combustion chamber, expander, heat supplier, second expander, regenerator, third expander, air compressor, smoke machine and second smoke machine; externally, there is an air passage which is communicated with the coke burning-regeneration system 2 through the air compressor 12 and the heat source regenerator 1, the coke burning-regeneration system 2 also has a flue gas passage which is communicated with the outside through the smoke machine 13, the heat exchanger 4 and the heat source regenerator 1, the coke burning-regeneration system 2 also has a CO-rich flue gas passage which is communicated with the combustion chamber 5 through the second smoke machine 14, the combustion chamber 5 also has a flue gas passage which is communicated with the outside through the heat exchanger 4 and the heat source regenerator 1, the outside has a low-temperature heat medium passage which is communicated with the compressor 3, the second expander 8 has a low-temperature heat medium passage which is communicated with the regenerator 9 and then communicated with the compressor 3 through the intermediate port, the compressor 3 also has a low-temperature heat medium passage which is communicated with the expander 6 through the heat exchanger 4 and the combustion chamber 5, the expander 6 also has a low-temperature heat medium passage which is divided into two routes after being communicated with the heat supplier 7, the first route is communicated with the second expander 8 and the second route is communicated with the regenerator 9, the regenerator 9 also has a low-temperature heat medium passage which is communicated with the outside through the third expander 10; the heat supplier 7 also has a heated medium passage which is communicated with the outside, the expander 6, the second expander 8 and the third expander 10 are connected with the compressor 3 and transmit power, the smoke machine 13 and the second smoke machine 14 are connected with the air compressor 12 and transmit power.

[0057] (2) Compared with the catalyst regeneration energy recovery heat pump system shown in Figure 1 , the difference is that: the outside air flows through the air compressor 12 to increase pressure and temperature, then flows through the heat source regenerator 1 to absorb heat and increase temperature, and then enters the coke burning-regeneration system 2; the flue gas discharged from the coke burning-regeneration system 2 flows through the smoke machine 13 to reduce pressure and work, and then is provided to the heat exchanger 4; the CO-rich flue gas discharged from the coke burning-regeneration system 2 flows through the second smoke machine 14 to reduce pressure and work, and then is provided to the combustion chamber 5; the mechanical energy output by the expander 6, the second expander 8, the third expander 10, the smoke machine 13 and the second smoke machine 14 is provided to the compressor 3 and the air compressor 12 as power, or the mechanical energy output by the expander 6, the second expander 8, the third expander 10, the smoke machine 13 and the second smoke machine 14 is provided to the compressor 3, the air compressor 12 and the outside as power, or the expander 6, the second expander 8, the third expander 10, the smoke machine 13, the second smoke machine 14 and the outside jointly provide power to the compressor 3 and the air compressor 12, forming the catalyst regeneration energy recovery heat pump system.

[0058] Figure 6 The catalyst regeneration energy recovery heat pump system shown in

[0059] In Figure 5The shown catalyst regeneration energy recovery heat pump system, externally added fuel passage is communicated with combustion chamber 5;Fuel and rich CO flue gas combustion in combustion chamber 5 produces high temperature flue gas, high temperature flue gas releases heat to the low temperature heat medium flowing through combustion chamber 5, and then provides heat exchanger 4;The increased fuel provides high temperature driving heat load through combustion chamber 5, forming a catalyst regeneration energy recovery heat pump system.

[0060] Figure 7 The shown catalyst regeneration energy recovery heat pump system is realized as follows:

[0061] (1) structurally, in Figure 5 The shown catalyst regeneration energy recovery heat pump system, increase auxiliary combustion chamber 11, externally have fuel passage and auxiliary combustion chamber 11 communication, adjust the flue gas passage of coking-regeneration system 2 and smoke machine 13 communication to the flue gas passage of coking-regeneration system 2 and auxiliary combustion chamber 11 communication, auxiliary combustion chamber 11 again flue gas passage and smoke machine 13 communication.

[0062] (2) process, compared with Figure 5 The shown catalyst regeneration energy recovery heat pump system, the difference is that: external fuel enters auxiliary combustion chamber 11, the flue gas discharged by coking-regeneration system 2 enters auxiliary combustion chamber 11, fuel and flue gas combustion in auxiliary combustion chamber 11 forms higher temperature flue gas, and then provides smoke machine 13, forming a catalyst regeneration energy recovery heat pump system.

[0063] Figure 8 The shown catalyst regeneration energy recovery heat pump system is realized as follows:

[0064] (1) structurally, in Figure 1 The shown catalyst regeneration energy recovery heat pump system, increase second regenerator, adjust the low temperature heat medium passage outside the compressor 3 communication to the low temperature heat medium passage outside the compressor 3 communication through second regenerator 15, adjust the low temperature heat medium passage of regenerator 9 and external communication through third expander 10 to the low temperature heat medium passage of regenerator 9 and external communication through second regenerator 15 and third expander 10.

[0065] (2) process, compared with Figure 1 The shown catalyst regeneration energy recovery heat pump system, the difference is that: external low temperature heat medium flows through second regenerator 15 and absorbs heat to rise temperature, and then enters compressor 3 to rise pressure and temperature;The second low temperature heat medium discharged by heat supplier 7 flows through regenerator 9 and second regenerator 15 and gradually releases heat to reduce temperature, and then enters third expander 10 to reduce pressure and work, and then discharges externally, forming a catalyst regeneration energy recovery heat pump system.

[0066] Figure 9The catalyst regeneration energy recovery heat pump system shown is implemented as follows:

[0067] (1) Structurally, in Figure 1 In the catalyst regeneration energy recovery heat pump system shown, a second regenerator is added. The external low-temperature heat medium channel connected to the compressor 3 is adjusted to be connected to the compressor 3 via the second regenerator 15. The regenerator 9 is adjusted to be connected to the third expander 10 via the low-temperature heat medium channel, and then the third expander 10 is connected to itself via the second regenerator 15 via the low-temperature heat medium channel.

[0068] (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 low-temperature heat medium flows through the second regenerator 15 to absorb heat and increase temperature, and then enters the compressor 3 to increase pressure and temperature; the low-temperature heat medium enters the third expander 10 to reduce pressure and do work, and after reaching a certain level, it flows through the second regenerator 15 to release heat and decrease temperature, and then enters the third expander 10 to continue to reduce pressure and do work, and then is discharged to the outside, forming the catalyst regeneration energy recovery heat pump system.

[0069] Figure 10 The catalyst regeneration energy recovery heat pump system shown is implemented as follows:

[0070] (1) Structurally, in Figure 1 In the catalyst regeneration energy recovery heat pump system shown, a dehumidifying heat exchanger and a gas-liquid separator are added. The third expander 10 is adjusted so that it has a low-temperature heat medium channel connected to the outside, which is connected to itself via the dehumidifying heat exchanger 16 and the gas-liquid separator 17. Then the third expander 10 has a low-temperature heat medium channel connected to the outside. The dehumidifying heat exchanger 16 also has a cooling medium channel connected to the outside, and the gas-liquid separator 17 also has a condensate pipeline connected to the outside.

[0071] (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: the low-temperature heat medium enters the third expander 10 to reduce pressure and perform work. After reaching a certain level, it flows through the dehumidification heat exchanger 16 to release heat and cool down, and condensate is precipitated. Then, it enters the gas-liquid separator 17 for gas-liquid separation. The condensate is discharged to the outside. The separated low-temperature heat medium enters the third expander 10 to continue to reduce pressure and perform work and be discharged to the outside, forming the catalyst regeneration energy recovery heat pump system.

[0072] Figure 11 The catalyst regeneration energy recovery heat pump system shown is implemented as follows:

[0073] (1) Structurally, in Figure 1The catalyst regeneration energy recovery heat pump system shown in the figure is realized as follows:(1) In the catalyst regeneration energy recovery heat pump system shown in the figure, a low-temperature heat exchanger 18 is added, the external low-temperature heat medium passage connected with the compressor 3 is adjusted to an external air passage connected with the compressor 3 through the low-temperature heat exchanger 18, the low-temperature heat medium passage of the low-temperature heat exchanger 18 is connected with the outside, and the low-temperature heat medium passage of the third expander 10 connected with the outside is changed to an air passage of the third expander 10 connected with the outside.

[0074] (2) Compared with the catalyst regeneration energy recovery heat pump system shown in the figure, the difference is that the external air flows through the low-temperature heat exchanger 18 to absorb heat and rise in temperature, and then enters the compressor 3 to rise in pressure and temperature; the low-temperature heat medium enters the third expander 10 to reduce pressure and work, and after a certain degree, flows through the low-temperature heat exchanger 18 to release heat and cool down and separate condensate, and then enters the gas-liquid separator 17 to separate gas and liquid - the condensate is discharged to the outside, and the low-temperature heat medium after separation enters the third expander 10 to continue to reduce pressure and work and discharge to the outside, forming the catalyst regeneration energy recovery heat pump system. Figure 1

[0075] Figure 12 The catalyst regeneration energy recovery heat pump system shown in the figure is realized as follows:

[0076] (1) In the catalyst regeneration energy recovery heat pump system shown in the figure, a low-temperature heat exchanger 18 is added, the external low-temperature heat medium passage connected with the compressor 3 is adjusted to an external air passage connected with the compressor 3 through the low-temperature heat exchanger 18, the low-temperature heat medium passage of the low-temperature heat exchanger 18 is connected with the outside, and the low-temperature heat medium passage of the third expander 10 connected with the outside is changed to an air passage of the third expander 10 connected with the outside. Figure 1 (2) Compared with the catalyst regeneration energy recovery heat pump system shown in the figure, the difference is that the external air flows through the low-temperature heat exchanger 18 to absorb heat and rise in temperature, and then enters the compressor 3 to rise in pressure and temperature; the low-temperature heat medium enters the third expander 10 to reduce pressure and work, and after a certain degree, flows through the low-temperature heat exchanger 18 to release heat and cool down and separate condensate, and then enters the gas-liquid separator 17 to separate gas and liquid - the condensate is discharged to the outside, and the low-temperature heat medium after separation enters the third expander 10 to continue to reduce pressure and work and discharge to the outside, forming the catalyst regeneration energy recovery heat pump system.

[0077] Figure 1 The catalyst regeneration energy recovery heat pump system shown in the figure is realized as follows:

[0078] Figure 13 (1) In the catalyst regeneration energy recovery heat pump system shown in the figure, a low-temperature heat exchanger 18 is added, the external low-temperature heat medium passage connected with the compressor 3 is adjusted to an external air passage connected with the compressor 3 through the low-temperature heat exchanger 18, the low-temperature heat medium passage of the low-temperature heat exchanger 18 is connected with the outside, and the low-temperature heat medium passage of the third expander 10 connected with the outside is changed to an air passage of the third expander 10 connected with the outside.

[0079] (1) In the catalyst regeneration energy recovery heat pump system shown in the figure, a low-temperature heat exchanger 18 is added, the external low-temperature heat medium passage connected with the compressor 3 is adjusted to an external air passage connected with the compressor 3 through the low-temperature heat exchanger 18, the low-temperature heat medium passage of the low-temperature heat exchanger 18 is connected with the outside, and the low-temperature heat medium passage of the third expander 10 connected with the outside is changed to an air passage of the third expander 10 connected with the outside. Figure 1 ​The catalyst regeneration energy recovery heat pump system shown in the figure is realized as follows:

[0080] (2) Compared with the catalyst regeneration energy recovery heat pump system shown in the figure, the difference is that: the external air flows through the dehumidification heat exchanger 16 and the low-temperature heat exchanger 18 to gradually absorb heat and warm up, and then enters the compressor 3 to increase pressure and temperature; the air enters the third expander 10 to reduce pressure and work, to a certain extent, flows through the dehumidification heat exchanger 16 to release heat and cool down and precipitate condensate, and then enters the gas-liquid separator 17 to carry out gas-liquid separation - the condensate is discharged to the outside, and the separated air enters the third expander 10 to continue to reduce pressure and work and discharge to the outside; the low-temperature heat medium passes through the low-temperature heat exchanger 18 to provide low-temperature heat load, forming the catalyst regeneration energy recovery heat pump system. Figure 1

[0081] Figure 14 The catalyst regeneration energy recovery heat pump system shown in the figure is realized as follows:

[0082] (1) In the catalyst regeneration energy recovery heat pump system shown in the figure, a high-temperature regenerator 19 is added, and the low-temperature heat medium passage of the compressor 3 is connected to the heat exchanger 4 through the high-temperature regenerator 19. Figure 1 (2) Compared with the catalyst regeneration energy recovery heat pump system shown in the figure, the difference is that: the low-temperature heat medium discharged by the compressor 3 flows through the high-temperature regenerator 19 to absorb heat and warm up, and then is provided to the heat exchanger 4: the low-temperature heat medium discharged by the expander 6 flows through the high-temperature regenerator 19 to release heat and cool down, and then is provided to the heat supply device 7, forming the catalyst regeneration energy recovery heat pump system.

[0083] Figure 1 The catalyst regeneration energy recovery heat pump system shown in the figure is realized as follows:

[0084] Figure 15 (1) In the catalyst regeneration energy recovery heat pump system shown in the figure, a high-temperature regenerator 19 is added, and the low-temperature heat medium passage of the compressor 3 is connected to the heat exchanger 4 through the high-temperature regenerator 19.

[0085] (1) In the catalyst regeneration energy recovery heat pump system shown in the figure, a high-temperature regenerator 19 is added, and the low-temperature heat medium passage of the compressor 3 is connected to the heat exchanger 4 through the high-temperature regenerator 19. Figure 1 ​​The shown catalyst regeneration energy recovery heat pump system, increase high temperature regenerator 19, the low temperature heat medium passage of compressor 3 is adjusted to be communicated with heat exchanger 4, the low temperature heat medium passage of compressor 3 is adjusted to be communicated with heat exchanger 4 through high temperature regenerator 19, the low temperature heat medium passage of expander 5 is adjusted to be communicated with heater 6 through high temperature regenerator 19, and the low temperature heat medium passage of expander 5 is further communicated with heater 6 after the low temperature heat medium passage of expander 5 is communicated with itself.

[0086] (2) Compared with the catalyst regeneration energy recovery heat pump system shown in the figure, the difference is that the low-temperature heat medium discharged by the compressor 3 flows through the high-temperature regenerator 19 to absorb heat and rise in temperature, and then is supplied to the heat exchanger 4; the low-temperature heat medium discharged by the combustion chamber 5 enters the expander 6 to work under pressure, and after a certain degree, flows through the high-temperature regenerator 19 to release heat and drop in temperature, enters the expander 6 to continue to work under pressure, and then is supplied to the heater 7, forming a catalyst regeneration energy recovery heat pump system. Figure 1

[0087] The technical effects that can be achieved by the present application are as follows:

[0088] (1) The technical measures for improving the heat energy grade of the catalyst regeneration process and utilizing refrigeration / heat are proposed.

[0089] (2) The temperature difference irreversible loss of the catalyst regeneration process is reduced, and the temperature of the initial driving heat source is improved.

[0090] (3) The temperature of the driving heat load is obtained, so that the performance index of the gas heat pump system is improved by increasing the heat absorption temperature.

[0091] (4) The driving heat load provided by the regeneration flue gas and the regeneration CO-rich flue gas is utilized in stages, the systematic irreversible loss is reduced, and the catalyst regeneration energy utilization level is improved.

[0092] (5) The fuel (such as refinery gas or purchased fuel) provides high-temperature driving heat load through the combustion chamber, greatly improving the refrigeration / heat value of the regeneration flue gas energy.

[0093] (6) The high-efficiency / high-value utilization of flue gas energy is realized by relatively simple technical measures, the cost is reduced, and the economy is improved.

[0094] (7) The regenerative measures improve the average temperature of the heat pump system during heat absorption, the systematic temperature difference loss is small, and the device performance index is improved.

[0095] (8) Multiple technical solutions are provided, which are beneficial to better improve the energy application value of the catalyst regeneration energy recovery heat pump system.​

Claims

1. The catalyst regeneration energy recovery heat pump system mainly consists of a heat source regenerator, a coke-regeneration system, a compressor, a heat exchanger, a combustion chamber, an expander, a heater, a second expander, a regenerator, and a third expander; 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 (4) and the heat source regenerator (1), the coke-regeneration system (2) also has a CO-rich flue gas passage connecting to the combustion chamber (5), the combustion chamber (5) also has a flue gas passage connecting to the outside via the heat exchanger (4) and the heat source regenerator (1), an external low-temperature heat medium passage connects to the compressor (3), and the second expander (8) has a low-temperature heat medium passage connecting to the compressor (3). After the heat medium channel connects to the regenerator (9), it is connected to the compressor (3) through the intermediate port. The compressor (3) also has a low-temperature heat medium channel that connects to the expander (6) through the heat exchanger (4) and the combustion chamber (5). The expander (6) also has a low-temperature heat medium channel that connects to the heater (7) and then splits into two paths - the first path connects to the second expander (8) and the second path connects to the regenerator (9). The regenerator (9) also has a low-temperature heat medium channel that connects to the outside through the third expander (10). The heater (7) also has a heated medium channel that connects to the outside. The expander (6), the second expander (8) and the third expander (10) are connected to the compressor (3) 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 (5) to form the catalyst regeneration energy recovery heat pump system.

3. The catalyst regeneration energy recovery heat pump system is a catalyst regeneration energy recovery heat pump system according to claim 1 or claim 2, wherein the heat source regenerator (1) is connected to the coke-regeneration system (2) by an air channel, and the heat source regenerator (1) is divided into two paths by an air channel - the first path is connected to the coke-regeneration system (2) and the second path is connected to the combustion chamber (5), thus forming the catalyst regeneration energy recovery heat pump system.

4. The catalyst regeneration energy recovery heat pump system is an auxiliary combustion chamber (11) added to any of the catalyst regeneration energy recovery heat pump systems described in claims 1-3. An external fuel channel is connected to the auxiliary combustion chamber (11). The coke-regeneration system (2) is adjusted so that the coke-regeneration system (2) is connected to the heat exchanger (4) through a flue gas channel. The auxiliary combustion chamber (11) is then connected to the heat exchanger (4) through a flue gas channel, thus forming the catalyst regeneration energy recovery heat pump system.

5. The catalyst regeneration energy recovery heat pump system mainly consists of a heat source regenerator, a coke-regeneration system, a compressor, a heat exchanger, a combustion chamber, an expander, a heater, a second expander, a regenerator, a third expander, an air compressor, a flue gas fan, and a second flue gas fan; externally, there is an air channel that connects to the coke-regeneration system (2) via the air compressor (12) and the heat source regenerator (1). The coke-regeneration system (2) also has a flue gas channel that connects to the outside via the flue gas fan (13), the heat exchanger (4), and the heat source regenerator (1). The coke-regeneration system (2) also has a CO-rich flue gas channel that connects to the combustion chamber (5) via the second flue gas fan (14). The combustion chamber (5) also has a flue gas channel that connects to the outside via the heat exchanger (4) and the heat source regenerator (1). Externally, there is a low-temperature heat medium channel that connects to the compressor (3). The second expander (8) After the low-temperature heat medium channel connects to the regenerator (9), it is connected to the compressor (3) through the intermediate port. The compressor (3) also has a low-temperature heat medium channel that connects to the expander (6) through the heat exchanger (4) and the combustion chamber (5). The expander (6) also has a low-temperature heat medium channel that connects to the heater (7) and then splits into two paths - the first path connects to the second expander (8) and the second path connects to the regenerator (9). The regenerator (9) also has a low-temperature heat medium channel that connects to the outside through the third expander (10). The heater (7) also has a heated medium channel that connects to the outside. The expander (6), the second expander (8) and the third expander (10) are connected to the compressor (3) and transmit power. The smoke machine (13) and the second smoke machine (14) are connected to the air compressor (12) and transmit power, forming a catalyst regeneration energy recovery heat pump system.

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

7. The catalyst regeneration energy recovery heat pump system is an auxiliary combustion chamber (11) added to the catalyst regeneration energy recovery heat pump system described in claim 5 or claim 6. The auxiliary combustion chamber (11) is connected to the external fuel channel. The coke-regeneration system (2) is adjusted to have a flue gas channel connected to the smoke machine (13) so that the coke-regeneration system (2) has a flue gas channel connected to the auxiliary combustion chamber (11) and the auxiliary combustion chamber (11) has a flue gas channel connected to the smoke machine (13), thus forming the 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 1-7, wherein a second regenerator is added, and the external low-temperature heat medium channel connected to the compressor (3) is adjusted to the external low-temperature heat medium channel connected to the compressor (3) through the second regenerator (15), and the regenerator (9) connected to the outside through the third expander (10) is adjusted to the regenerator (9) connected to the outside through the second regenerator (15) and the third expander (10), 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 1-7, wherein a second regenerator is added, and the external low-temperature heat medium channel connected to the compressor (3) is adjusted to the external low-temperature heat medium channel connected to the compressor (3) via the second regenerator (15), and the regenerator (9) connected to the third expander (10) via the low-temperature heat medium channel is adjusted to the regenerator (8) connected to the third expander (10), and then the third expander (10) is connected to itself via the second regenerator (15) via the low-temperature heat medium channel, 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 1-9, with the addition of a dehumidifying heat exchanger and a gas-liquid separator. The third expander (10) is adjusted so that the low-temperature heat medium channel is connected to the outside, and the third expander (10) has a low-temperature heat medium channel connected to itself through the dehumidifying heat exchanger (16) and the gas-liquid separator (17). Then the third expander (10) has a low-temperature heat medium channel connected to the outside. The dehumidifying heat exchanger (16) also has a cooling medium channel connected to the outside, and the gas-liquid separator (17) also has a condensate pipeline connected to the outside, thus 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, with the addition of a dehumidifying heat exchanger and a gas-liquid separator. The external low-temperature heat medium channel connected to the compressor (3) is adjusted to be connected to the compressor (3) via the dehumidifying heat exchanger (16). The low-temperature heat medium channel of the third expander (10) is adjusted to be connected to the outside via the dehumidifying heat exchanger (16) and the gas-liquid separator (17). After the third expander (10) is connected to itself via the dehumidifying heat exchanger (16) and the gas-liquid separator (17), the third expander (10) is connected to the outside via the low-temperature heat medium channel. The gas-liquid separator (17) is also connected to the outside via a condensate pipeline, thus forming a catalyst regeneration energy recovery heat pump system.

12. 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 low-temperature heat exchanger (18) is added, and the external low-temperature heat medium channel connected to the compressor (3) is adjusted to an external air channel connected to the compressor (3) via the low-temperature heat exchanger (18), the low-temperature heat exchanger (18) also has a low-temperature heat medium channel connected to the outside, and the third expander (10) having a low-temperature heat medium channel connected to the outside is changed to the third expander (10) having an air channel connected to the outside, thus forming a catalyst regeneration energy recovery heat pump system.

13. 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, with the addition of a dehumidifying heat exchanger, a gas-liquid separator and a low-temperature heat exchanger. The external low-temperature heat medium channel connected to the compressor (3) is adjusted to be connected to the compressor (3) via an external air channel through the dehumidifying heat exchanger (16) and the low-temperature heat exchanger (18). The third expander (10) is adjusted to be connected to the outside via a low-temperature heat medium channel through an air channel through the dehumidifying heat exchanger (16) and the gas-liquid separator (17) and then connected to itself. The third expander (10) also has an air channel connected to the outside. The gas-liquid separator (17) also has a condensate pipeline connected to the outside. The low-temperature heat exchanger (18) also has a low-temperature heat medium channel connected to the outside, thus forming a catalyst regeneration energy recovery heat pump system.

14. A catalyst regeneration energy recovery heat pump system is a catalyst regeneration energy recovery heat pump system according to any one of claims 7-8, with the addition of a dehumidifying heat exchanger and a gas-liquid separator. The external low-temperature heat medium channel is connected to the compressor (3) through the second regenerator (15) and adjusted to the external low-temperature heat medium channel being connected to the compressor (3) through the dehumidifying heat exchanger (16) and the second regenerator (15). The low-temperature heat medium channel of the third expander (10) is connected to the outside and adjusted to the third expander (10) having a low-temperature heat medium channel connected to itself through the dehumidifying heat exchanger (16) and the gas-liquid separator (17). After that, the third expander (10) has a low-temperature heat medium channel connected to the outside and the gas-liquid separator (17) also has a condensate pipeline connected to the outside, thus forming a catalyst regeneration energy recovery heat pump system.

15. A catalyst regeneration energy recovery heat pump system is a catalyst regeneration energy recovery heat pump system according to any one of claims 7-8, wherein a low-temperature heat exchanger is added, and the external low-temperature heat medium channel is connected to the compressor (3) through the second regenerator (15) to the external air channel being connected to the compressor (3) through the low-temperature heat exchanger (18) and the second regenerator (15). The low-temperature heat medium channel of the third expander (10) is changed to be connected to the outside, and the third expander (10) is connected to the outside air channel. The low-temperature heat exchanger (18) is also connected to the outside low-temperature heat medium channel, thus forming a catalyst regeneration energy recovery heat pump system.

16. A catalyst regeneration energy recovery heat pump system is a catalyst regeneration energy recovery heat pump system according to any one of claims 7-8, with the addition of a dehumidifying heat exchanger, a gas-liquid separator, and a low-temperature heat exchanger. The external low-temperature heat medium channel is connected to the compressor (3) through the second regenerator (15) and is adjusted to have an external air channel connected to the compressor (3) through the dehumidifying heat exchanger (16), the low-temperature heat exchanger (18), and the second regenerator (15). The low-temperature heat medium channel of the third expander (10) is connected to the outside and is adjusted to have an air channel connected to itself through the dehumidifying heat exchanger (16) and the gas-liquid separator (17). After that, the third expander (10) has an air channel connected to the outside, the gas-liquid separator (17) also has a condensate pipeline connected to the outside, and the low-temperature heat exchanger (18) also has a low-temperature heat medium channel connected to the outside, thus forming a catalyst regeneration energy recovery heat pump system.

17. A catalyst regeneration energy recovery heat pump system is a catalyst regeneration energy recovery heat pump system according to any one of claims 1-16, wherein a high-temperature regenerator (19) is added, the compressor (3) is connected to the heat exchanger (4) via a low-temperature heat medium channel, and the compressor (3) is connected to the heat exchanger (4) via the high-temperature regenerator (19), and the expander (5) is connected to the heater (6) via a low-temperature heat medium channel, and the expander (5) is connected to the heater (6) via the high-temperature regenerator (19), thereby forming a catalyst regeneration energy recovery heat pump system.

18. A catalyst regeneration energy recovery heat pump system is a catalyst regeneration energy recovery heat pump system according to any one of claims 1-16, wherein a high-temperature regenerator (19) is added, the compressor (3) is connected to the heat exchanger (4) via a low-temperature heat medium channel, and the compressor (3) is connected to the heat exchanger (4) via the high-temperature regenerator (19), and the expander (5) is connected to the heater (6) via a low-temperature heat medium channel, and the expander (5) is connected to itself via the high-temperature regenerator (19), and then the expander (5) is connected to the heater (6) via a low-temperature heat medium channel, thereby forming a catalyst regeneration energy recovery heat pump system.

Images