CN1746559A

CN1746559A - Coupled and heat-exchange heat supply with wide-range output

Info

Publication number: CN1746559A
Application number: CN 200510003141
Authority: CN
Inventors: 保廷荣
Original assignee: Individual
Current assignee: Individual
Priority date: 2005-07-26
Filing date: 2005-07-26
Publication date: 2006-03-15
Anticipated expiration: 2025-07-26
Also published as: CN100357659C

Abstract

In the invention, the heating system consists of a heater, a super-heater, an evaporator, a steam-water separator, a flow mixer, an automatic flow control valve, a temperature-sensing element and a pipe fitting member. The super-heater and the evaporator are connected to be a coupler, which is used for the two mediums- water and high boiling point liquor coupling heat exchange. The high boiling point medium is heated by the heater, then heat exchanged with the water medium via the heater and the evaporator, at last go back to the heater so as to form the circular flowing procedure. The water medium flows into the evaporator, then the superheated steam is output after evaporating via the steam-water separator, the super-heater and the flow mixer so as to form the procedure of producing the superheated steam by water. The saturation steam flow is regulated by an automatic flow control valve and the temperature-sensing element is adjusted, so as to realize the width-range temperature output.

Description

The coupled and heat-exchange heat supply with wide-range output method

Technical field

The present invention is relevant with steam superheating, and is especially relevant with the steam heating that with heating means is characteristics, in particular to the coupled and heat-exchange heat supply with wide-range output method.

Background technology

Existing heat-supplying mode has multiple heat-supplying modes such as steam heating, high-temperature medium heat supply, electric heating, the direct heating of combustion gas.Wherein the steam heating mode is by widespread usage.But adopt steam heating to be subjected to the restriction of China's boiler manufacturing standard: evaporation capacity is exported less than the low steam of can only realizing at a lower temperature of boiler pressure parameter of 8t/h.Because most of steam boilers are not established superheating system, thereby will improve the pressure parameter of the output temperature of steam with regard to necessary raising boiler, cause equipment investment excessive thus, security reliability descends.Some need the higher occasion of temperature parameter then to adopt directly mode of heating such as electric heating, combustion gas.These mode thermals efficiency are low, are not easy to UTILIZATION OF VESIDUAL HEAT IN.For overcoming this weakness, some producers have adopted the heat-supplying mode of high-temperature medium heat transfer, but because the consideration of aspects such as safety, the heater operated by rotary motion is in the place away from workshop; And high-temperature medium viscosity big, be not suitable for remote conveying, thereby seldom be used.Therefore how to use the hyperthermia and superheating steam heating, be a difficult problem always.In the existing technology of applying for a patent, only there is No. 89102458.12 " superheated steam temperature difference heating process classification and equipment thereof " to propose in heating process more than 160 ℃, to use the technical scheme of superheated steam heat supply, yet this scheme only is suitable for printing and dyeing industry, does not occur better heat supply scheme at present as yet.

Summary of the invention

The objective of the invention is to overcome the deficiency of above-mentioned technology, provide a kind of have a two media coupling characteristics of heat transfer can be at the heat supply method of realizing overtemperature adjustable output of working medium temperature wide cut in 100～400 ℃ of scopes under normal pressure and the low pressure condition, to satisfy in the production field heat supply needs that high temperature and temperature required wide ranges, temperature switched frequent system.

The method that the inventor provides comprises:

(1) heating system is connected to form by equipment such as heater, superheater, evaporimeter, steam-water separator, mixed flow device and motor valve, temperature-sensing element, pipe fitting;

(2) heating system adopts two media, and a kind of is water, and another kind is the higher boiling liquid;

(3) system makes coupling device with the device that superheater, evaporimeter connect to form, and aqueous medium and high boiling medium are carried out coupled and heat-exchange;

(4) high boiling medium is heated by heater, by superheater, evaporimeter and aqueous medium heat exchange, gets back to heater, forms the flow process of circular flow;

(5) aqueous medium enters evaporimeter, steam-water separator, superheater, mixed flow device by make-up water, exports superheated steam then, forms the flow process by aquatic product superheated steam;

(6) temperature control signals that provides by the temperature-sensing element of being located at mixed flow device exit of system, and the saturated vapor flow is regulated, thereby to regulate the heat distribution ratio between evaporimeter and the superheater and to regulate the temperature wide cut way of output that saturated vapor and the mixing ratio realization of superheated steam are regulated system's output temperature by being located between steam-water separator and the mixed flow device motor valve on the direct piping.

(7) system regulates the blowdown presssure of fixed gas by the pressure regulator valve of being located on the expansion oil sealing, to regulate the boiling point of high boiling medium, makes that the temperature difference between the high boiling medium and aqueous medium satisfies overheated needs in the coupler.

Described heater is a radiation indirect heating apparatus, and it can adopt, and any mode heats high boiling medium in combustion gas, fire coal, fuel oil, the electric heating.

Described superheater and evaporimeter are two sections overlapped tubular heat exchangers, and its epimere is a superheater, and hypomere is an evaporimeter, and high boiling medium passes through in managing, and aqueous medium is evaporated to steam and is heated between pipe.

Described steam-water separator is an airtight tubular equipment, on cylindrical shell, from top to bottom set up saturated vapor efferent duct, mist input pipe, recirculated water input pipe separately, its effect is that saturated vapor is separated with unevaporated aqueous medium, and steam is sent into superheater, and water flows into evaporimeter; Cylindrical shell is provided with the water level meter that links to each other with this steam-water separator outward, with the liquid level of reflection evaporimeter.

Described mixed flow device is a kind of two sections different pipes of diameter to be connected to form concentric reducer with one section Taper Pipe, establish shrouding at the major part of pipe, a base is established in perforate on shrouding, establish a base on the major part tube wall, the member that forms a threeway shape is described mixed flow device; Be provided with motor valve between steam-water separator and the mixed flow device.

Described high boiling medium is superheater cylinder oil or castor oil, also can have higher boiling, liquid that viscosity is little with other.

The present invention is owing to adopted the coupling device that superheater and evaporimeter are coupled together, utilization two media coupled and heat-exchange combines with the temperature adjusting mode, preferably resolve the wide cut output problem of heating system temperature under normal pressure low pressure, overcome that pipeline in the simple dependence high boiling medium heat-supplying mode is long, resistance is big, the insecure disadvantage of heat supply, overcome the steam generator system that adopts single heat exchange mode preferably and obtained the necessary increase of high temperature output boiler pressure, thus the disadvantage that causes security reliability to descend.The present invention can be in the heat supply that realizes overtemperature adjustable output of working medium temperature wide cut in 100～400 ℃ of scopes under normal pressure and the low pressure condition, reliable operation, security performance are good, low equipment investment, thermal efficiency height, be convenient to UTILIZATION OF VESIDUAL HEAT IN, applied widely, the exploitation that can be new products such as environmental protection, chemical industry provides the ideal experimental facilities thermal source, can be production fields such as environmental protection, chemical industry, biology the thermal source of being convenient to control that satisfies multiple needs is provided.

Description of drawings

Accompanying drawing is the principle schematic of coupled and heat-exchange heat supply with wide-range output method.Among the figure: 1 for taking over, and 2 are high boiling medium input base, and 3 is heater, 4 are high boiling medium output base, 5 for taking over, and 6 are high boiling medium input base, and 7 is end cap, 8 is blast pipe, 9 is pressure regulator valve, and 10 are the expansion oil sealing, and 11 are superheated steam output base, 12 is the mixed flow device, 13 is temperature-sensing element, 14 is motor valve, 15 are the straight-through output of saturated vapor base, 16 are saturated vapor bypass output base, 17 are saturated vapor input base, 18 are mist input base, and 19 is the water level meter, and 20 are mist output base, 21 are recirculated water input base, 22 for recirculated water exports base down, and 23 is make-up water input base, and 24 are the water inlet base, 25 are the blowdown base, 26 are high boiling medium output base, and 27 are recirculated water output base, and 28 is steam-water separator, 29 is evaporimeter, and 30 is superheater.

The specific embodiment

The coupled and heat-exchange heat supply with wide-range output system is made up of heater 3, superheater 30, evaporimeter 29, steam-water separator 28, mixed flow device 12, motor valve 14, temperature-sensing element 13 and pipe fitting member as shown in drawings; Adopt two media, a kind of is water, and another kind is overheated cylinder oil; System makes coupling device with the device that superheater 30, evaporimeter 29 connect to form, and aqueous medium and overheated cylinder oil are carried out coupled and heat-exchange; Overheated cylinder oil by superheater 30, evaporimeter 29 and aqueous medium heat exchange, is got back to heater 3 by fuel heater 3 heating, forms the flow process of circular flow; Aqueous medium enters evaporimeter 29 by make-up water, flashes to behind the steam by steam-water separator 28, superheater 30, mixed flow device 12, and the output superheated steam forms the flow process by aquatic product superheated steam; System regulates by being located between steam-water separator 28 and the mixed flow device 12 14 pairs of saturated vapor flows of the motor valve on the direct piping, to regulate the mixing ratio of saturated vapor and superheated steam, adjust temperature-sensing element 13, can realize the temperature wide cut way of output that temperature is regulated in 100～400 ℃ of scopes.System regulates by the blowdown presssure of being located at the 9 pairs of fixed gases of pressure regulator valve on the expansion oil sealing 10, to regulate the boiling point of high boiling medium, makes that the temperature difference between the high boiling medium and aqueous medium satisfies overheated needs in the coupling device.

Its operation principle is: high boiling medium is heated back increase in temperature proportion in heater 3 reduces along high boiling medium output base 4, take over 5, high boiling medium input base 6 enters superheater 30, evaporimeter 29, in superheater 30, carry out heat exchange with the gas phase of aqueous medium, in evaporimeter 29, carry out heat exchange with the liquid phase of aqueous medium, temperature reduce high boiling medium that proportion increases by high boiling medium output base 26, take over 1, high boiling medium input base 2 enters heater 3 circulation of finishing the work.

Aqueous medium enters evaporimeter 29 by make-up water input base 23, make-up water input pipe 24, and obtain heat vaporization therein, mist is entered steam-water separator 28 carbonated drink in steam-water separator 28 and is separated by mist output base 20, mist input base 18, saturated vapor by saturated vapor bypass efferent duct 16 flow out through saturated vapor input base 17 enter superheater 30 in superheater 30 by overheated, superheated steam is flowed out by superheated steam efferent duct 11 and enters mixed flow device 12, exports from mixed flow device 12 microcephaly's outputs.

Adjust the control temperature of temperature-sensing element 13, when the vapor (steam) temperature of output is higher than temperature-sensing element 13 control temperature, motor valve 14 is opened automatically, and saturated vapor enters mixed flow device 12 by the straight-through output of saturated vapor base 15 and mixes the required output temperature control of realization with the superheated steam of importing mixed flow devices 12 by superheated steam output base 11.Outlet base 22, make-up water input base 23, water inlet base 24 make evaporimeter 29 be communicated with steam-water separator 28, thereby make water level meter 19 can reliably reflect the liquid level of evaporimeter 29 under recirculated water efferent duct 27, recirculated water input base 21, the recirculated water being provided with between evaporimeter 29 and the steam-water separator 28.

Claims

1 coupled and heat-exchange heat supply with wide-range output method, its feature comprises:

1. heating system is made up of heater (3), superheater (30), evaporimeter (29), steam-water separator (28), mixed flow device (12), motor valve (14), temperature-sensing element (13) and pipe fitting member;

2. heating system adopts two media, and a kind of is water, and another kind is the higher boiling liquid;

3. system makes coupling device with the device that superheater (30), evaporimeter (29) connect to form, and aqueous medium and high boiling medium are carried out coupled and heat-exchange;

4. high boiling medium by superheater (30), evaporimeter (29) and aqueous medium heat exchange, is got back to heater (3) by heater (3) heating, forms the flow process of circular flow;

5. aqueous medium enters evaporimeter (29), flashes to behind the steam by steam-water separator (28), superheater (30), mixed flow device (12), and the output superheated steam forms the flow process by aquatic product superheated steam;

6. the temperature control signals that provides by the temperature-sensing element (13) of being located at mixed flow device exit of system, and the saturated vapor flow is regulated, thereby to regulate the heat distribution ratio between evaporimeter and the superheater and to regulate the temperature wide cut way of output that saturated vapor and the mixing ratio realization of superheated steam are regulated system's output temperature by being located between steam-water separator (28) and the mixed flow device (12) motor valve (14) on the direct piping.

7. system regulates the blowdown presssure of fixed gas by the pressure regulator valve of being located on the expansion oil sealing (10) (9), to regulate the boiling point of high boiling medium, makes that the temperature difference between the high boiling medium and aqueous medium satisfies overheated needs in the coupler.

2 coupled and heat-exchange heat supply with wide-range output methods according to claim 1, it is characterized in that described heater (3) is a radiation indirect heating apparatus, it adopts a kind of mode in combustion gas or coal-fired or fuel oil or the electric heating that high boiling medium is heated.

3 coupled and heat-exchange heat supply with wide-range output methods according to claim 1, it is characterized in that described superheater (30) and evaporimeter (29) are two sections overlapped tubular heat exchangers, its epimere is superheater (30), hypomere is evaporimeter (29), high boiling medium passes through in managing, and aqueous medium flows between pipe.

4 coupled and heat-exchange heat supply with wide-range output methods according to claim 1, it is characterized in that described steam-water separator (28) is an airtight tubular equipment, from top to bottom sets up saturated vapor efferent duct (17), mist input pipe (27), recirculated water input pipe (22) separately on cylindrical shell; Cylindrical shell is provided with the water level meter (19) that links to each other with this steam-water separator (28) outward.

5 coupled and heat-exchange heat supply with wide-range output methods according to claim 1, it is characterized in that described mixed flow device (12) is two sections concentric reducers that the different pipe of diameter connects to form with one section Taper Pipe, its microcephaly is that the port of export is provided with the member of establishing superheated steam efferent duct (15) the threeway shape that forms on temperature-sensing element (13), its major part; Be provided with motor valve (14) between steam-water separator (28) and the mixed flow device (12).

6 coupled and heat-exchange heat supply with wide-range output methods according to claim 1 is characterized in that described high boiling medium is superheater cylinder oil or castor oil.