CN214147838U - Industrial steam supply deep thermoelectric decoupling system - Google Patents
Industrial steam supply deep thermoelectric decoupling system Download PDFInfo
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- CN214147838U CN214147838U CN202022959772.1U CN202022959772U CN214147838U CN 214147838 U CN214147838 U CN 214147838U CN 202022959772 U CN202022959772 U CN 202022959772U CN 214147838 U CN214147838 U CN 214147838U
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Abstract
The utility model discloses an industry supplies vapour degree of depth thermoelectric decoupling zero system, including boiler, high pressure cylinder, intermediate pressure cylinder, low pressure cylinder, condenser and ejector to through temperature reduction and pressure reduction unit, throttle the regulating element, heating unit, shutoff unit and contrary unit connection that ends. The invention can realize the stability and the persistence of industrial steam supply in the adjusting range with larger power generation load, realize the matching operation of the power generation load of the unit and the dispatching of the power grid, and meet the requirement of the industrial steam supply operation of the large-scale unit generator set.
Description
Technical Field
The utility model relates to a thermoelectric decoupling zero system, concretely relates to industry steam feed degree of depth thermoelectric decoupling zero system belongs to combined heat and power generation technical field.
Background
Large-scale thermal power generating set generally adopts the unit system, promptly: turbo generator and boiler one-to-one compares with the main control of most industry garden thermal power plant, and this kind of configuration mode has good controllability and economic nature when pure congealing the electricity generation, but when supplying steam for industrial enterprise as the thermal power plant, has more problems.
Because of high steam pressure, industrial steam supply is generally extracted from a plurality of places such as high-pressure cylinder exhaust steam, a reheater outlet or a superheater outlet (new steam), but no matter where steam is extracted, the load matching problem of a boiler reheater and a superheater is brought, the superheater steam comes from a boiler drum, and the through-flow steam quantity is equal to the water supply quantity in principle. The reheater steam comes from the steam exhaust of the high-pressure cylinder of the steam turbine, and is equal to the new steam amount minus the steam extraction of the high-pressure regenerative heater, the steam extraction of the shaft seal, the air leakage of the main valve and the like, under the pure condensing power generation condition, the through-flow steam amount of the reheater and the through-flow steam amount of the superheater are basically considered to be in a fixed proportional relation, that is, if the steam is extracted from the steam exhaust of the high-pressure cylinder or the outlet of the superheater for industrial steam supply, the through-flow steam amount of the reheater must be reduced, so that the ratio of the through-flow steam amount of the reheater and the through-flow steam amount of the superheater is unbalanced, the heat exchange area, the arrangement position and the like of the reheater and the superheater during the boiler construction are designed and cannot be adjusted and changed at will inevitably, if the through-flow steam amount of the reheater is reduced, the reheater will be overheated inevitably caused, and subsequent heating surfaces such as an economizer, an air preheater and the like are high temperature, and the boiler safety is influenced.
If industrial steam supply is extracted from the outlet of the reheater, the problem of load matching of through-flow steam volume of the reheater and the superheater is solved, and the mismatching of the steam inlet of the high-pressure cylinder and the intermediate-pressure cylinder of the steam turbine is caused.
Steam flows in a turbine and can generate axial force on a turbine rotor, under normal conditions, steam inlet quantities of a high-pressure cylinder and a medium-pressure cylinder of the turbine have a fixed proportional relation, and through measures of different shaft shoulders at steam inlet and steam outlet positions, different designs of reaction degrees of movable blades of the medium-pressure cylinder and the high-pressure cylinder, and the like, under a pure condensation working condition, the high-pressure cylinder and the medium-pressure cylinder can ensure axial thrust balance under any load condition, so if steam is extracted from an outlet of a reheater for supplying heat, the steam inlet quantity of the high-pressure cylinder is greater than the steam inlet quantity of the medium-pressure cylinder, axial thrust imbalance is caused, steam extraction from the steam outlet of the high-pressure cylinder can also cause the phenomenon, the axial thrust of the high-pressure cylinder and the medium-pressure cylinder is unbalanced, a thrust bearing is caused to be high.
In addition, the extraction pressure is closely related to the load of the steam turbine at the high-pressure cylinder exhaust, reheater outlet and other places: the lower the load of the steam turbine is, the lower the extraction pressure is, and for the occasion that the industrial steam supply pressure requirement is greater than 1.8MPa, the high-pressure cylinder steam discharge pressure cannot be met when the load of most steam turbines is less than 60%, that is, if stable industrial steam supply is maintained, the load of a steam turbine unit for extracting steam and supplying heat needs to be maintained at a high level, but the load is limited by a power grid, for example, during the valley electricity at night, the supply and demand of the power grid are balanced, and the power generation load of the steam turbine is controlled below 40%.
Therefore, the large-scale unit-made power generating unit is changed into an industrial heat supply unit, which has a larger problem, especially when the heat supply load is larger, so that a new technology and a new method need to be developed to fundamentally solve the large-scale industrial steam supply problem of the large-scale unit-made thermal power generating unit and realize deep thermoelectric decoupling.
SUMMERY OF THE UTILITY MODEL
The to-be-solved technical problem of the utility model is to overcome the above-mentioned not enough of prior art, provide an industry steam supply degree of depth thermoelectric decoupling zero system.
In order to solve the above problem, the utility model adopts the following technical scheme: an industrial steam supply depth thermoelectric decoupling system comprises a boiler, a high-pressure cylinder, a medium-pressure cylinder, a low-pressure cylinder, a condenser and an ejector, and is connected with a non-return unit through a temperature and pressure reducing unit, a throttling adjusting unit, a heating unit, a breaking unit and a non-return unit.
The following is the utility model discloses to the further optimization of above-mentioned scheme: the temperature and pressure reduction unit comprises a temperature and pressure reduction device a, a temperature and pressure reduction device b, a temperature and pressure reduction device C and a temperature and pressure reduction device d.
Further optimization: the throttling regulation unit comprises a throttling regulation valve A, a throttling regulation valve D, a throttling regulation valve F, a throttling regulation valve C and a throttling regulation valve L.
Further optimization: the blocking unit comprises a blocking valve E, a blocking valve I, a blocking valve J, a blocking valve B, a blocking valve G, a blocking valve H, a blocking valve M, a blocking valve K, a blocking valve A, a blocking valve B, a blocking valve C, a blocking valve D and a blocking valve F.
Further optimization: the check unit comprises a first check valve, a second check valve, a third check valve and a fourth check valve.
Further optimization: the heating unit comprises a heater I, a heater II and a shaft seal heater.
Further optimization: the boiler includes a reheater and a superheater.
Further optimization: the reheater is connected with an interruption valve A, an interruption valve B, an interruption valve I, a throttling regulating valve D and a temperature-reducing pressure reducer D, the interruption valve A is connected with the temperature-reducing pressure reducer C, the interruption valve B is connected with the temperature-reducing pressure reducer B, the interruption valve I is connected with an ejector, the ejector is connected with an interruption valve J, the interruption valve J8 is connected with a medium pressure cylinder, the ejector is connected with the interruption valve C and the throttling regulating valve C, a second check valve is connected with the interruption valve C, the throttling regulating valve C is connected with the interruption valve B, the interruption valve B is connected with a third check valve, the third check valve is connected with the reheater, the throttling regulating valve D is connected with a first check valve, the first check valve is connected with a high pressure cylinder, a steam inlet of the first check valve and the high pressure cylinder is connected with a superheater through the throttling regulating valve A, the interruption valve D is connected between the throttling regulating valve A and the third check valve, and the interruption valve D is connected with the temperature-reducing pressure reducer a, an interruption valve B and a third check valve are connected with a high-pressure cylinder, a temperature reduction pressure reducer d is connected with an interruption valve E, the interruption valve E is communicated with a medium-pressure cylinder through a throttling regulating valve F, a fourth interruption valve is communicated between the interruption valve E and the throttling regulating valve F, the fourth interruption valve is communicated with the interruption valve B, an interruption valve H and a throttling regulating valve C through an interruption valve G, the interruption valve C is connected with a low-pressure cylinder, the low-pressure cylinder is connected with a condenser, the condenser is connected with a throttling regulating valve L and a shaft seal heater, a condensate pump is arranged between the shaft seal heater and the condenser, the heater is connected with a heater I through a three-way valve, the heater I is connected with a low-pressure regenerative heating system through the interruption valve F, the heater I is connected with an interruption valve K through an interruption valve M, the interruption valve M and the interruption valve K are connected with a medium steam exhaust port, the interruption valve K is connected with the condenser through the throttling regulating valve L, the heater I is connected with a deaerator through a heater II, and the heater II is connected with a blocking valve H.
The utility model discloses can realize that industry supplies stable, lasting of vapour in the great control range of power generation load, realize that unit power generation load and electric wire netting dispatch match the operation, satisfy large-scale unit system generating set industry and supply vapour operation requirement.
The present invention will be further explained with reference to the drawings and examples.
Drawings
Fig. 1 is a flow chart of the present invention in an embodiment;
fig. 2 is a flow chart of an injection operation mode in the embodiment of the present invention;
fig. 3 is a flow chart of the joint debugging operation mode in the embodiment of the present invention.
In the figure: 1. temperature and pressure reducers C, 2, throttle regulating valves A, 3, throttle regulating valves D, 4, temperature and pressure reducers D, 5, throttle regulating valves F, 6, blocking valves E, 7, blocking valves I, 8, blocking valves J, 9, temperature and pressure reducers B, 10, an ejector, 11, an intermediate pressure cylinder, 12, an intermediate pressure cylinder exhaust port, 13, a low pressure cylinder, 14, a low pressure cylinder steam inlet port, 15, temperature and pressure reducers a, 16, a reheater outlet port, 17, a superheater, 18, a reheater, 19, a reheater inlet, 20, a high pressure cylinder, 21, a high pressure cylinder exhaust port, 22, a high pressure cylinder steam inlet port, 23, an intermediate pressure cylinder steam inlet port, 24, blocking valves B, 25, blocking valves G, 26, blocking valves H, 27, heaters II, 28, throttle regulating valves C, 29, blocking valves M, 30, heaters I, 31, blocking valves K, 32, throttle regulating valves L, 33, three-way valves 34, and a heater, 35. a condenser; 36. an interruption valve A; 37. an interruption valve B; 38. an interruption valve C; 39. an interruption valve D; 40. an interruption valve F; 41-a first check valve; 42-a second check valve; 43-a third check valve; 44-fourth check valve.
Detailed Description
In the embodiment, as shown in fig. 1-3, an industrial steam supply deep thermoelectric decoupling system includes a boiler, a reheater 18 and a superheater 17 are disposed on the boiler, a reheater outlet 16 and a reheater inlet 19 are disposed on the reheater 18, the reheater outlet 16 is connected to an interruption valve a36, an interruption valve B37, an interruption valve I7, a throttle regulating valve D3 and a temperature and pressure reducing device D4 through pipes, the other end of the interruption valve a36 is connected to a temperature and pressure reducing device C1 through pipes, the other end of the temperature and pressure reducing device C1 is connected to a small steam turbine and a deaerator, the other end of the interruption valve B37 is connected to a temperature and pressure reducing device B9 through pipes, steam output by the temperature and pressure reducing device B9 is used for industrial steam supply, the other end of the interruption valve I7 is connected to an injector 10 through a pipe, the injector 10 is provided with two input ends and one output end, one of which is connected to the interruption valve I7, and the other input end (low-pressure injector end) is connected to one end of the interruption valve J8, the other end of the blocking valve J8 is connected with the steam exhaust port 12 of the intermediate pressure cylinder and the second check valve 42 on the intermediate pressure cylinder 11 through pipelines, the output end of the ejector 10 is respectively connected with one end of the blocking valve C38 and one end of the throttling regulating valve C28, the other end of the second check valve 42 is connected with the other end of the blocking valve C38, the other end of the throttling regulating valve C28 is connected with one end of the blocking valve B24 through pipelines, the other end of the blocking valve B24 is connected with one end of the third check valve 43 through pipelines, the other end of the third check valve 43 is connected with the inlet 19 of the reheater through pipelines, the other end of the throttling regulating valve D3 is connected with one end of the first check valve 41, the other end of the first check valve 41 is connected with the steam inlet port 22 of the high pressure cylinder 20 through pipelines, the steam inlet port 22 of the first check valve 41 and the high pressure cylinder is connected with the output end of the throttling regulating valve A2, the blocking valve D39 is connected between the superheater A2 and the third check valve 43 through a bypass pipeline, a temperature and pressure reducing device a15 is connected between the blocking valve D39 and the third check valve 43, the blocking valve B24 and the third check valve 43 are connected with the high-pressure cylinder steam exhaust port 21 on the high-pressure cylinder 20, the other end of the temperature and pressure reducing device D4 is connected with one end of the blocking valve E6 through a pipeline, the blocking valve E6 is communicated with the medium-pressure cylinder steam inlet port 23 on the medium-pressure cylinder 11 through a throttle regulating valve F5, the blocking valve E6 and the throttle regulating valve F5 are communicated through a communication pipeline, the fourth check valve 44 is communicated with the blocking valve B24, the blocking valve H26 and the throttle regulating valve C28 through a blocking valve G25, one end of the blocking valve C38 far away from the second check valve 42 is connected with the low-pressure cylinder steam inlet port 14 on the low-pressure cylinder 13, the low-pressure cylinder 13 is connected with a condenser 35, the condenser 35 is connected with a throttle regulating valve L32 and a condenser heater 34, a shaft seal 34 is arranged between the condenser 35, and the shaft seal heater 34 is connected with a three-way valve I through a three-way valve I30, the heater I30 is connected with a low-pressure regenerative heating system through an interruption valve F40, the heater I30 is connected with an interruption valve K31 through an interruption valve M29, the interruption valve M29 and the interruption valve K31 are connected with the exhaust port 12 of the intermediate pressure cylinder, the interruption valve K31 is connected with the condenser 35 through a throttle regulating valve L32, the heater I30 is connected with a deaerator through a heater II 27, and the heater II 27 is further connected with an interruption valve H26.
The first check valve 41 is open along the direction from the reheater outlet 16 to the steam inlet 22 of the high-pressure cylinder, otherwise;
the second check valve 42 is communicated along the direction from the steam exhaust port 12 of the intermediate pressure cylinder to the steam inlet port 14 of the low pressure cylinder, and vice versa;
the third check valve 43 is communicated along the direction from the high-pressure cylinder steam exhaust port 21 to the reheater inlet 19, otherwise;
the fourth check valve 44 is opened along the direction from the high pressure cylinder exhaust port 21 to the intermediate pressure cylinder inlet port, and vice versa.
The temperature and pressure reducer a15, the temperature and pressure reducer b9, the temperature and pressure reducer C1 and the temperature and pressure reducer d4 form a temperature and pressure reducing unit.
The throttle regulating valve A2, the throttle regulating valve D3, the throttle regulating valve F5, the throttle regulating valve C28 and the throttle regulating valve L32 form a throttle regulating unit.
The blocking unit consists of a blocking valve E6, a blocking valve I7, a blocking valve J8, a blocking valve B24, a blocking valve G25, a blocking valve H26, a blocking valve M29, a blocking valve K31, a blocking valve A36, a blocking valve B37, a blocking valve C38, a blocking valve D39 and a blocking valve F40.
The first check valve 41, the second check valve 42, the third check valve 43 and the fourth check valve 44 form a check unit.
The heater I30, the heater II 27 and the shaft seal heater 34 form a heating unit.
Simultaneously the utility model also discloses a use method of industry steam supply degree of depth thermoelectric decoupling zero system, this method is according to the relation between power generation load and the steam supply load, through the switching of above-mentioned interconnection pipeline, valve, and this system divide into draws and penetrates the operational mode and allies oneself with transfers the operational mode to satisfy the thermoelectric decoupling zero requirement of degree of depth.
When the power generation load is lower, an injection operation mode is adopted:
at the moment, the throttle valve A2 on the new steam pipeline is closed, the temperature and pressure reducing device a15 and the blocking valve D39 are opened, the new steam is bypassed to the reheater inlet 19 through temperature and pressure reduction, and the circulating steam quantity between the reheater 18 and the superheater 17 is balanced;
at the moment, the steam entering the high-pressure cylinder 20 is led out from the reheater outlet 16 pipeline and enters the high-pressure cylinder 20 through the throttle regulating valve D3 and the check valve 41; the high pressure cylinder 20 has low exhaust steam pressure and cannot flow into the reheater inlet 19, at this time, the blocking valve B24 is opened, part of the steam flows to the low pressure cylinder 13 through the throttle regulating valve C28, part of the steam enters the heater II 27 through the blocking valve H26 to heat condensed water, and the blocking valve G25 communicated with a communication pipeline between the steam inlet 23 of the medium pressure cylinder is closed; the high-pressure steam on the side of the reheater 18 is prevented from flowing back through the check valve 43 between the steam outlet 21 of the high-pressure cylinder and the inlet 19 of the reheater, the steam entering the intermediate pressure cylinder 11 is led from the pipeline of the outlet 16 of the reheater through the blocking valve E6 and the throttle regulating valve F5; a part of the steam discharged by the intermediate pressure cylinder 11 is injected and pressurized by an injector 10 and is discharged to the low pressure cylinder 13 from a steam inlet 14 of the low pressure cylinder, and the other part of the steam is led to a heater I30 through a shutoff valve M29 to heat condensed water; wherein, the driving steam of the ejector 10 is led from the steam at the outlet 16 of the reheater, the industrial steam supply is led out from the pipeline at the outlet 16 of the reheater 18 and is supplied out by temperature and pressure reduction, and the steam for the small steam turbine and the deaerator is led out from the pipeline at the outlet 16 of the reheater and is supplied out by the temperature and pressure reduction C1;
in this operation mode, the boiler feed water enters the boiler, and finally new steam is produced by the superheater 17, and the throttle valve a2 is closed, so that all the new steam enters the reheater inlet 19 through the shutoff valve D39 and the temperature and pressure reducer a 15; the steam is heated by a reheater 18 and exhausted to a reheater outlet 16; the steam at the outlet 16 of the reheater is divided into five parts, wherein one part of the steam is supplied to a small steam turbine and a deaerator through a temperature and pressure reducer C1, one part of the steam is supplied to industrial steam supply through a temperature and pressure reducer b9, one part of the steam is supplied to the ejector 10 through a shutoff valve I7, one part of the steam is supplied to the intermediate pressure cylinder 11 through a temperature and pressure reducer D4, and the last part of the steam is supplied to the high pressure cylinder 20 through a throttle valve D3;
steam at the outlet 16 of the reheater enters the high-pressure cylinder 20 through a throttle valve D3, a check valve 41 and a high-pressure cylinder steam inlet 22 to push the high-pressure cylinder 20 to work, the steam exhaust at the high-pressure cylinder steam outlet 21 is divided into 2 strands through a blocking valve B24, one strand is discharged to the low-pressure cylinder 13 through a throttle valve C28, and the other strand is supplied to a heater II 27 through a blocking valve H26 to heat condensed water; steam at the outlet 16 of the reheater enters the intermediate pressure cylinder 11 through a temperature and pressure reducing device d4, a blocking valve E6 and a throttle control valve F5 to push the intermediate pressure cylinder 11 to do work, the exhaust steam of the intermediate pressure cylinder 11 is divided into 2 strands through two intermediate pressure cylinder exhaust ports 12, one strand is injected and pressurized through a blocking valve J8 and exhausted to the low pressure cylinder 13, and the other strand is supplied to a heater I30 through a blocking valve M29 to heat condensed water; steam from the ejector 10 is converged into the low pressure cylinder 13 by exhaust steam of the high pressure cylinder 20 from the throttle control valve C28, the low pressure cylinder 13 is pushed to do work, the exhaust steam of the low pressure cylinder 13 enters the condenser 35 to be condensed into condensed water, enters the shaft seal heater 34, is heated by the heater I30 and the heater II 27 and is sent to the deaerator, and the steam-water flow is completed;
in this mode of operation, the principle method of deep thermoelectric decoupling is: the new steam is subjected to temperature reduction and pressure reduction, and is bypassed to a reheater inlet 19, so that the steam flow balance between a reheater 18 and a superheater 17 is realized; the steam inlet source of the high pressure cylinder 20 is adjusted from the live steam to the reheater outlet 16 (reheated steam hot section), and since the inlet pressure is greatly reduced, the steam inlet flow of the high pressure cylinder 20 is also greatly reduced according to the fledgle's formula, thereby reducing the work load of the high pressure cylinder 20; in order to make the high pressure cylinder 20 exhaust steam smoothly, the high pressure cylinder 20 exhausts steam to the low pressure cylinder 13; after the steam inlet amount and the steam inlet pressure of the high-pressure cylinder 20 are reduced, in order to balance the axial thrust balance of the intermediate-pressure cylinder 11 and the high-pressure cylinder 20, a throttle regulating valve F5 is additionally arranged at the steam inlet of the intermediate-pressure cylinder 11 to regulate the steam inlet pressure and the steam inlet flow of the intermediate-pressure cylinder 11; in order to make the steam exhaust of the intermediate pressure cylinder 11 smooth, the steam exhaust of the intermediate pressure cylinder 11 is lifted by the ejector 10 and then introduced into the low pressure cylinder 13 or used for heating condensed water; in order to ensure that the steam feed pump and the deaerator work normally, steam is led out from an outlet 16 of the reheater and is supplied out through temperature reduction and pressure reduction; industrial steam supply load is adjusted through a temperature and pressure reducer b 9; the power generation load is adjusted through the throttle regulating valve D3, the throttle regulating valve F5 and the ejector 10, when the power generation load requirement is improved, the throttle regulating valve D3 is opened to increase the steam admission of the high pressure cylinder 20, and the throttle regulating valve F5 is adjusted to realize axial thrust balance and adjust the ejector 10 to ensure that the steam admission and steam exhaust pressure ratio of the intermediate pressure cylinder 11 is within the range required by the intermediate pressure cylinder 11; when the requirement of the power generation load is lower, the throttle regulating valve D3 is turned down, and the throttle regulating valve F5 and the regulating ejector 10 are adjusted at the same time.
When the power generation load is higher, a joint debugging operation mode is adopted:
at this time, the throttle control valve A2 on the new steam pipeline is opened, and the steam entering the high-pressure cylinder 20 comes from the new steam; at this time, the inlet steam pressure of the high-pressure cylinder 20 is higher than the pressure at the outlet 16 of the reheater, and the check valve 41 behind the throttle regulating valve D3 is closed to prevent new steam from entering the pipeline at the outlet 16 of the reheater; the blocking valve B24 at the steam outlet 21 of the high-pressure cylinder is closed, the steam outlet pressure of the high-pressure cylinder 20 is increased, and the steam enters the inlet 19 of the reheater through the check valve 43; the steam inlet of the intermediate pressure cylinder 11 still leads steam from the outlet 16 of the reheater, an interruption valve J8, an interruption valve K31 and an interruption valve M29 connected to the steam outlet 12 of the intermediate pressure cylinder are closed, all the steam discharged by the intermediate pressure cylinder 11 enters the low pressure cylinder 13, and the ejector 10 stops working; the desuperheater-depressor a15 and the shutoff valve D39 are still open, bypassing a portion of the live steam to the reheater inlet 19;
in the operation mode, boiler feed water enters a boiler, new steam is finally generated by the superheater 17, and the throttle control valve A2 is opened, so that part of the new steam enters the high-pressure cylinder 20 and pushes the high-pressure cylinder 20 to do work, and part of the new steam enters the reheater inlet 19 through the temperature and pressure reducer a 15; at the moment, the blocking valve B24 is closed, and all the exhausted steam of the high-pressure cylinder 20 enters the inlet 19 of the reheater; the steam is heated by a reheater 18 and exhausted to a reheater outlet 16; the steam output from the outlet 16 of the reheater is divided into two parts, one part is supplied to industrial steam supply through a temperature and pressure reducer b9, the other part is supplied to the intermediate pressure cylinder 11 through a temperature and pressure reducer d4, an interruption valve E6 and a throttling regulating valve F5 and pushes the intermediate pressure cylinder 11 to do work, the exhaust steam of the intermediate pressure cylinder 11 is discharged to the low pressure cylinder 13 and pushes the low pressure cylinder 13 to do work, the exhaust steam of the low pressure cylinder 13 enters a condenser 35 to be condensed into condensed water and enters a shaft seal heater 34, and then the condensed water passes through a turbine original low pressure regenerative heating system to complete steam-water circulation;
in this mode of operation, the principle method of deep thermoelectric decoupling is: the temperature and the pressure of the new steam are reduced, the new steam is bypassed to an inlet of a reheater 18, and the steam flow balance between the reheater 18 and a superheater 17 is realized; the steam inlet source of the high pressure cylinder 20 is adjusted to the new steam from the reheater outlet 16 (reheated steam hot section), and since the inlet pressure is greatly increased, the steam inlet flow of the high pressure cylinder 20 is also greatly increased according to the fledgle's formula, thereby increasing the work done by the high pressure cylinder 20; industrial steam supply load is adjusted through a temperature and pressure reducer b 9; the power generation load is adjusted through the throttle adjusting valve A2, when the power generation load requirement is higher, the throttle adjusting valve A2 is opened to be larger, the steam admission of the high-pressure cylinder 20 is increased, and the throttle adjusting valve F5 is adjusted simultaneously for realizing the axial thrust balance of the high-pressure cylinder 20 and the intermediate-pressure cylinder 11; when the power generation load requirement is lower, the throttle regulating valve A2 is turned down, and the throttle regulating valve F5 is adjusted to realize the axial thrust balance of the high pressure cylinder 20 and the intermediate pressure cylinder 11; the temperature and pressure reducer a15 is used for adjusting the exhaust pressure of the high-pressure cylinder 20, and the ratio of the exhaust pressure of the high-pressure cylinder 20 to the pressure of the high-pressure cylinder 20 after the adjustment stage is maintained between 0.45 and 0.55.
Switching the joint debugging operation mode to the injection operation mode:
in the joint debugging operation mode, when the power generation load is continuously reduced so that the exhaust pressure of the high-pressure cylinder 20 cannot meet the industrial steam supply requirement, switching to the injection operation mode is required;
at the moment, the throttle regulating valve A2 is gradually closed, the blocking valve B24, the blocking valve K31 and the throttle regulating valve D3 are opened at the same time, the steam inlet pressure and the steam outlet pressure of the high-pressure cylinder 20 are matched and regulated through the throttle regulating valve C28, the ratio of the steam outlet pressure of the high-pressure cylinder 20 to the pressure after regulation is maintained to be 0.4-0.45, the steam inlet pressure and the steam outlet pressure of the intermediate-pressure cylinder 11 are matched and regulated through the throttle regulating valve L32, and the ratio of the steam outlet pressure and the steam inlet pressure of the intermediate-pressure cylinder 11 is maintained to be 0.23-0.27; meanwhile, the opening degree of the temperature and pressure reducing device a15 is increased (increased), the pressure at the outlet 16 of the reheater is kept stable, the boiler output is increased, and the new steam pressure is kept stable; after the throttle regulating valve A2 is completely closed, the blocking valve J8 and the blocking valve I7 are opened, the ejector 10 is opened, the blocking valve M29, the blocking valve H26 and the three-way valve 33 are simultaneously opened, the heater I30 and the heater II 27 are started, the throttle regulating valve L32 is gradually closed under the condition that the steam exhaust pressure and the steam inlet pressure ratio of the intermediate pressure cylinder 11 are not lower than 0.23 and not higher than 0.27, and therefore the joint regulation operation mode is switched to the ejection operation mode.
The injection operation mode is switched to the joint debugging operation mode:
in the injection operation mode, when the throttle regulating valve D3 is fully opened and still cannot meet the requirement for increasing the power generation load, the operation mode needs to be switched to the joint debugging operation mode;
at this time, the temperature and pressure reducer d4 is adjusted to make the opening degree of the throttle adjusting valve F5 reach 100%, and the axial thrust of the high pressure cylinder 20 and the intermediate pressure cylinder 11 is balanced and adjusted by the temperature and pressure reducer d 4; opening a blocking valve G25, gradually opening a throttle regulating valve A2 at the same time, improving the steam inlet pressure of the high-pressure cylinder 20, performing matching regulation of the steam inlet pressure and the steam exhaust pressure of the high-pressure cylinder 20 through a throttle regulating valve C28, and maintaining the ratio of the steam exhaust pressure of the high-pressure cylinder 20 to the post-regulation pressure of 0.4-0.45; at this time, if the difference between the steam inlet temperature of the high pressure cylinder 20 and the steam inlet temperature of the intermediate pressure cylinder 11 is large (generally controlled within 30 ℃), the steam inlet temperature of the intermediate pressure cylinder 11 is properly reduced through the temperature and pressure reducer d 4; opening a blocking valve K31, and maintaining the exhaust pressure and the steam inlet pressure ratio of the intermediate pressure cylinder 11 between 0.23 and 0.27 through a throttle regulating valve L32; adjusting the load of the boiler to ensure that the new steam pressure is kept stable; when the exhaust pressure of the high-pressure cylinder 20 is higher than the pressure of the reheater inlet 19, the blocking valve B24 is closed; when the exhaust pressure of the intermediate pressure cylinder 11 is higher than the inlet pressure of the low pressure cylinder 13, the blocking valve I7, the blocking valve J8, the blocking valve M29 and the blocking valve K31 are closed, the condensed water three-way valve 33 is closed, and the system completes the switching of the joint adjusting operation mode.
In the switching process of the two operation modes, the principle method of deep thermoelectric decoupling is as follows: the new steam is subjected to temperature reduction and pressure reduction, and is bypassed to a reheater inlet 19, so that the steam flow balance between a reheater 18 and a superheater 17 is realized; after the steam inlet amount and the steam inlet pressure of the high-pressure cylinder 20 are changed, the steam inlet pressure and the steam inlet flow of the intermediate-pressure cylinder 11 are adjusted by the temperature and pressure reducer d4 in order to balance the axial thrust balance of the intermediate-pressure cylinder 11 and the high-pressure cylinder 20; in order to ensure that the steam feed pump and the deaerator work normally, steam is led out from an outlet 16 of the reheater and is supplied out through temperature reduction and pressure reduction; the industrial steam supply load is adjusted by the temperature and pressure reducer b 9.
For example, the following steps are carried out:
taking subcritical 330MW multiplied by 2 generator sets of a certain power plant as an example, the rated operation mode parameters of the boiler are as follows: the new steam amount is 1059t/h, the new steam temperature is 537 ℃, and the new steam pressure is 16.7 MPa; the reheat steam temperature is 537 ℃, and the reheat steam pressure is 3.9 MPa; the industrial steam supply pressure is 2.8MPa, and the industrial steam supply amount is 400 t/h.
In the power utilization peak period of a power grid in the daytime, if the power grid dispatching requires that the power generation load of a single unit is higher than 160MW (about 48% of the rated power generation load of the unit), 2 units need to operate according to a deep thermoelectric decoupling joint debugging operation mode under the condition of meeting the requirement of 400t/h of industrial steam supply;
at this time, throttle regulating valve a2 is adjusted according to the power generation load to regulate the steam entering high pressure cylinder 20; adjusting the temperature and pressure reducer a15 according to the exhaust pressure of the high pressure cylinder 20, and adjusting the exhaust pressure of the high pressure cylinder 20; in order to realize the axial thrust balance of the high-pressure cylinder 20 and the intermediate-pressure cylinder 11, the steam inlet pressure of the intermediate-pressure cylinder 11 is started and adjusted through the throttle regulating valve F5; the block valve B24, the block valve G25, the block valve I7, the block valve H26, the block valve M29, the block valve K31 and the block valve J8 are closed, and the temperature and pressure reducing device c1 is closed; the three-way valve 33 is closed, and the condensed water enters the low-pressure regenerative heating system of the original turbine after coming out of the shaft seal heater 35;
in the operation mode, boiler feed water enters a boiler, new steam is finally generated by the superheater 17, and the throttle control valve A2 is opened, so that part of the new steam enters the high-pressure cylinder 20 to push the high-pressure cylinder 20 to do work, and part of the new steam enters the reheater inlet 19 through the temperature and pressure reducer a 15; at the moment, the blocking valve B24 is closed, and all the exhausted steam of the high-pressure cylinder 20 enters the inlet 19 of the reheater; the steam is heated by a reheater 18 and exhausted to a reheater outlet 16; the steam at the outlet 16 of the reheater is divided into two parts, one part is supplied to industrial steam supply through a temperature and pressure reducer b9, the other part is supplied to the intermediate pressure cylinder 11 through a temperature and pressure reducer d4 and an interruption valve E6, the intermediate pressure cylinder 11 is pushed to do work, the exhaust steam of the intermediate pressure cylinder 11 is discharged to the low pressure cylinder 13, the low pressure cylinder 13 is pushed to do work, the exhaust steam of the low pressure cylinder 13 enters a condenser 35 to be condensed into condensed water, enters a shaft seal heater 34, and then enters an original low-pressure regenerative heating system of the steam turbine through a three-way valve 33, and steam-water circulation is completed;
under the joint regulation operation mode, the industrial steam supply amount of a single unit is maintained at 200t/h, the power generation load of the unit can be adjusted between 160 and 282MW, and the boiler load is adjusted within the range of 70-100%; wherein when the industrial steam supply of a single unit is 200t/h and the power generation load is 160MW (corresponding to the load rate of about 48%), the boiler load is 70%;
when the power grid dispatching requires that the power generation load of a single unit is lower than 160MW, the unit needs to be switched from a joint dispatching operation mode to an injection operation mode;
at the moment, closing the throttle regulating valve A2, simultaneously opening an interruption valve B25, an interruption valve K31, a throttle regulating valve D3, an interruption valve J8 and an interruption valve I7, opening the ejector 10, opening an interruption valve M29, an interruption valve H26 and a three-way valve 33, starting a heater I30 and a heater II 27, and starting a throttle regulating valve C28 and a throttle regulating valve L32; maintaining the pressure at the outlet 16 of the reheater to be stable, increasing (increasing) the opening of the temperature and pressure reducing device a15, increasing the boiler output, and maintaining the new steam pressure to be stable; after the throttle regulating valve A2 is completely closed, gradually closing the throttle regulating valve L32 under the condition that the pressure ratio of the exhaust steam pressure to the intake steam pressure of the intermediate pressure cylinder 11 is not lower than 0.23 and not higher than 0.27;
in this operation mode, the boiler feed water enters the boiler, and finally new steam is produced by the superheater 17, and the throttle valve a2 is closed, so that all the new steam enters the reheater inlet 19 through the temperature and pressure reducer a 15; the steam is heated by a reheater 18 and exhausted to a reheater outlet 16; the steam at the outlet 16 of the reheater is divided into five parts, wherein one part of the steam is supplied to a small steam turbine and a deaerator through a temperature and pressure reducer c1, one part of the steam is supplied to industrial steam supply through a temperature and pressure reducer b9, one part of the steam is supplied to the ejector 10 through a shutoff valve I7, one part of the steam is supplied to the intermediate pressure cylinder 11 through a temperature and pressure reducer D4, and the last part of the steam is supplied to the high pressure cylinder 20 through a throttle valve D3; steam at the outlet 16 of the reheater enters the high-pressure cylinder 20 through the throttling regulating valve D3 to push the high-pressure cylinder 20 to do work, the exhaust steam of the high-pressure cylinder 20 is divided into 2 strands after passing through the blocking valve B24, one strand is discharged to the low-pressure cylinder 13 through the throttling regulating valve C28, and the other strand is supplied to the heater II 27 through the blocking valve H26 to heat condensed water; steam at the outlet 16 of the reheater enters the intermediate pressure cylinder 11 through a temperature and pressure reducing device d4, an interruption valve E6 and a throttle control valve F5 to push the intermediate pressure cylinder 11 to do work, the exhaust steam of the intermediate pressure cylinder 11 is divided into 2 strands, one strand of the exhaust steam is pressurized and exhausted to the low pressure cylinder 13 through an interruption valve J8 and the ejector 10, and the other strand of the exhaust steam is supplied to a heater I30 through an interruption valve M29 to heat condensed water; steam from the ejector 10 is converged into the low pressure cylinder 13 from the high pressure cylinder 20 exhaust steam from the throttle control valve C32, the low pressure cylinder 13 is pushed to do work, the low pressure cylinder 13 exhaust steam enters the condenser to be condensed into condensed water, enters the shaft seal heater 34, is heated by the heater I30 and the heater II 27, and is sent to the deaerator, and the steam-water flow is completed.
Under the injection operation mode, the industrial steam supply amount of a single unit can be adjusted within the range of 0-600t/h, so that the industrial steam supply requirement can be met only by 1 unit of generator set, under the condition that the industrial steam supply amount of the single unit is 400t/h, the power generation load of the single unit can be adjusted within the range of 56-121MW, and the boiler load is adjusted within the range of 80-100%; wherein when the industrial steam supply of a single unit is 400t/h and the power generation load is 56MW, the boiler load is 80%;
if the single industrial steam supply is still maintained at 200t/h, the unit power generation load can be adjusted between 56 and 160MW, and the boiler load is adjusted within the range of 60 to 100 percent, wherein when the single unit industrial steam supply is 200t/h, the power generation load is 56MW (corresponding to the load rate of about 17 percent), the boiler load is 60 percent.
In the injection operation mode, if the power generation load requirement of the power grid dispatching on a single unit is increased to more than 160MW, the joint dispatching operation mode needs to be switched;
at this time, the temperature and pressure reducer d4 is adjusted to make the opening degree of the throttle adjusting valve F5 reach 100%, and the axial thrust of the high pressure cylinder 20 and the intermediate pressure cylinder 11 is balanced and adjusted by the temperature and pressure reducer d 4; opening a blocking valve G25, gradually opening a throttle regulating valve A2 at the same time, improving the steam inlet pressure of the high-pressure cylinder 20, performing matching regulation on the steam inlet pressure and the steam outlet pressure of the high-pressure cylinder 20 through a throttle regulating valve C28, and maintaining the steam outlet pressure of the high-pressure cylinder 20 to be 0.4-0.45 of the post-regulation pressure ratio; at this time, if the difference between the steam inlet temperature of the high pressure cylinder 20 and the air inlet temperature of the intermediate pressure cylinder 11 is large (exceeding 30 ℃), the steam inlet temperature of the intermediate pressure cylinder 11 is properly reduced through the temperature and pressure reducer d 4; opening a blocking valve K31, and maintaining the pressure ratio of the exhaust steam pressure to the intake steam pressure of the intermediate pressure cylinder 11 at 0.23-0.27 through a throttle regulating valve L32; adjusting the load of the boiler to ensure that the new steam pressure is kept stable; when the exhaust pressure of the high-pressure cylinder 20 is higher than the pressure of the reheater inlet 19, the blocking valve B24 is closed; when the exhaust pressure of the intermediate pressure cylinder 11 is higher than the inlet pressure of the low pressure cylinder 35, the blocking valve I7, the blocking valve J8, the blocking valve M29 and the blocking valve K31 are closed, the condensed water three-way valve 33 is closed, and the system completes the switching to the joint regulation operation mode.
The scheme realizes the reduction of the output power of the high-pressure cylinder 20 by reducing the steam inlet pressure of the high-pressure cylinder 20; the balance of the axial thrust of the high-pressure cylinder 20 and the axial thrust of the intermediate-pressure cylinder 11 is realized by adjusting the steam inlet pressure of the intermediate-pressure cylinder 11; the balance between the boiler reheater 18 and the superheater 17 is realized by bypassing the new steam after temperature and pressure reduction; the smooth steam discharge of the intermediate pressure cylinder 11 is realized by heating the condensed water and the ejector 10; lead to low pressure jar 13 through high pressure jar 20 steam exhausts, realize that high pressure jar 20 steam exhausts unobstructed, adopt above-mentioned technical measure, the utility model discloses can realize that the industry supplies stability, last of vapour in the great control range of power generation load, realize that unit power generation load and electric wire netting dispatch match the operation, satisfy large-scale unit system generating set industry and supply vapour operation requirement.
Having shown and described the basic principles and essential features of the invention and advantages thereof, it will be apparent to those skilled in the art that the invention is not limited to the details of the foregoing exemplary embodiments, but is capable of other specific forms without departing from the spirit or essential characteristics thereof, and it is therefore intended that the embodiments be considered as exemplary and not limiting in any way, since the scope of the invention is defined by the appended claims rather than by the foregoing description, and all changes which come within the meaning and range of equivalency of the claims are therefore intended to be embraced therein and are therefore not to be embraced therein by any reference numerals in the claims.
Claims (1)
1. An industrial steam supply deep thermoelectric decoupling system is characterized in that: the boiler comprises a boiler, a reheater and a superheater are arranged on the boiler, a reheater outlet and a reheater inlet are arranged on the reheater, an interruption valve A, an interruption valve B, an interruption valve I, a throttling regulating valve D and a temperature and pressure reducer D are connected to the outlet of the reheater, a temperature and pressure reducer C is connected to the other end of the interruption valve A, a temperature and pressure reducer B is connected to the other end of the interruption valve B, the other end of the interruption valve I is connected with an ejector, two input ends and one output end are arranged on the ejector, one input end is connected with the interruption valve I, the other input end is connected with one end of an interruption valve J, the other end of the interruption valve J is connected with a steam exhaust port of a middle pressure cylinder and a second check valve on the middle pressure cylinder, the output end of the ejector is respectively connected with one end of the interruption valve C and one end of the throttling regulating valve C, the other end of the second check valve is connected with the other end of the interruption valve C, one end of the interruption valve B is connected with the other end of the throttling regulating valve C, the other end of the blocking valve B is connected with one end of a third check valve through a pipeline, the other end of the third check valve is connected with an inlet of a reheater, the other end of a throttling regulating valve D is connected with one end of a first check valve, the other end of the first check valve is connected with a steam inlet of a high-pressure cylinder on the high-pressure cylinder, the steam inlets of the first check valve and the high-pressure cylinder are connected with a superheater through a throttling regulating valve A, a blocking valve D is connected between the throttling regulating valve A and the third check valve, a temperature reduction pressure reducer a is connected between the blocking valve D and the third check valve, the blocking valve B and the third check valve are connected with a steam outlet of the high-pressure reducer cylinder on the high-pressure cylinder, the other end of the temperature reduction valve D is connected with one end of a blocking valve E, the blocking valve E is communicated with a steam inlet of a medium-pressure cylinder on the medium-pressure cylinder through a throttling regulating valve F, a fourth check valve is communicated between the blocking valve E and the throttling regulating valve F, and the fourth check valve is communicated with the blocking valve B, Shut-off valve H and throttle governing valve C intercommunication, shut-off valve C keeps away from the one end of second check valve and is connected with the low pressure jar steam inlet on the low pressure jar, be connected with the condenser on the low pressure jar, be connected with throttle governing valve L and bearing seal heater on the condenser, be provided with condensate pump between bearing seal heater and the condenser, the bearing seal heater has heater I through three-way valve connection, heater I is connected with low pressure backheat heating system through shut-off valve F, heater I is connected with shut-off valve K through shut-off valve M, shut-off valve M and shut-off valve K are connected with the steam vent of intermediate pressure jar, shut-off valve K is connected with the condenser through throttle governing valve L, heater I is connected with the oxygen-eliminating device through heater II, heater II still is connected with shut-off valve H.
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| Publication number | Priority date | Publication date | Assignee | Title |
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| CN115853608A (en) * | 2022-12-12 | 2023-03-28 | 东方电气集团东方汽轮机有限公司 | Steam turbine middle-connection door parameter adjusting heat supply system and method for improving steam flow of steam turbine middle-connection door parameter adjusting heat supply system |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
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| CN115853608A (en) * | 2022-12-12 | 2023-03-28 | 东方电气集团东方汽轮机有限公司 | Steam turbine middle-connection door parameter adjusting heat supply system and method for improving steam flow of steam turbine middle-connection door parameter adjusting heat supply system |
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