CN202864923U - Double-zone efficient device for recovering yellow phosphorus combustion heat energy - Google Patents
Double-zone efficient device for recovering yellow phosphorus combustion heat energy Download PDFInfo
- Publication number
- CN202864923U CN202864923U CN 201220554682 CN201220554682U CN202864923U CN 202864923 U CN202864923 U CN 202864923U CN 201220554682 CN201220554682 CN 201220554682 CN 201220554682 U CN201220554682 U CN 201220554682U CN 202864923 U CN202864923 U CN 202864923U
- Authority
- CN
- China
- Prior art keywords
- heat
- combustion zone
- communicated
- transmission
- convection
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Withdrawn - After Issue
Links
Images
Landscapes
- Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
Abstract
The utility model discloses a double-zone efficient device for recovering yellow phosphorus combustion heat energy, which sequentially comprises a bracket, a sufficient combustion zone component, a convection heat transfer zone component and a steam pocket from bottom to top, wherein one end of a descending pipe of a sufficient combustion zone is communicated with the steam pocket, and the other end is communicated with a lower connection box of the sufficient combustion zone component; one end of a water steam guide pipe of the sufficient combustion zone is communicated with the steam pocket, and the other end is communicated with an upper connection box of the sufficient combustion zone component; one end of a descending pipe of a convection heat transfer zone is communicated with the steam pocket, and the other end is communicated with a cooling water inlet pipe in the convection heat transfer zone component; one end of a water steam guide pipe of the convection heat transfer zone is communicated with the steam pocket, and the other end is communicated with a water steam outlet pipe in the convection heat transfer zone component; and a lower seal head of the sufficient combustion zone component is connected with the bracket. The device disclosed by the utility model can realize efficient recovery of the yellow phosphorus combustion heat energy of which the theoretical recovery rate can exceed 75%, promotes energy conservation and emission reduction in thermal phosphoric acid production, and has broad application prospects in thermal phosphoric acid production.
Description
Technical field
The utility model relates to a kind of heat energy generated during combustion of yellow and reclaims and use device, especially relates to a kind of device of two-region type high efficiente callback heat energy generated during combustion of yellow.
Background technology
Thermal phosphoric acid can reach the high purity more than 99.99%, thereby it is indispensable important foundation industrial chemicals in the national economy, in space flight and aviation, biochemical industry, electronic information, life science, the highly purified phosphoric acid of required high added value (as: food grade, pharmaceutical grade, electron-level phosphoric acid etc.) and the production of fine phosphate product all be unable to do without thermal phosphoric acid in many high-technology fields such as biological medicine.The biotechnological formulations such as vaccine " Tamiflu-Ro 64-0796/002 (Ao Erfei) " such as anti-first stream N1H1 all need to use highly purified thermal phosphoric acid to do raw material.Yet traditional thermal phosphoric acid production also is the industry of a highly energy-consuming.Production technique all adopts water or dilute phosphoric acid that yellow phosphorus reaction heat is taken away, and water and dilute phosphoric acid recycle after cooling, and the low grade heat energy (temperature is lower than 80 ℃) that this part is taken out of by water or acid can't further utilize; Simultaneously, special-purpose coal firing boiler also need be set on the production technique and provide steam for production.Form the utmost point un-reasonable phenomenon that had both needed the outside reaction heat of supplying with steam and self producing rationally to utilize in the production system and caused energy dissipation, not only increased consumption and the CO of water, electricity, coal resource
2, SO
2Isothermal chamber gas purging amount, and residual heat of reaction drains into atmosphere formation thermal pollution by recirculated water.Just because of existing highly energy-consuming and CO in the thermal phosphoric acid production
2Maximum discharge; international energy crisis and " capital of a country letter of agreement " developed country is reduced discharging caused under the dual-pressure that requires in the world some century-old phosphorous chemical industry manufacturing enterprises (as: German Hirst, Asia, French sieve ground, Britain's Albright Wilson's etc.) since last century the nineties withdraw from one after another phosphorus chemical industry, phosphorus chemical industry is married again developing country.The phosphate rock resource of China is positioned at the third place in the world, and this provided opportunity both for the development of Chinese phosphorus chemical industry, simultaneously also highly energy-consuming and CO
2The danger and disaster of discharging has imputed to China.Therefore, for Chinese phosphorous chemical industry enterprise, opportunity and danger and disaster coexistence.The key that makes phosphorous chemical industry enterprise obtain Sustainable development is " energy-saving and emission-reduction ", thoroughly changes the present situation of thermal phosphoric acid production highly energy-consuming.Waste heat recovery in the thermal phosphoric acid production has been one of emphasis power-saving technology of general character in the sulphur dioxide of phosphor chemical industry with utilizing technology.
For this present situation, people's whats such as the Song Yao ancestral of Tsing-Hua University have proposed the patent of invention (patent No.: ZL 01 143443.0) of " Phosphorus combustion heat recovery and utilization device and its thermal phosphoric acid production system " December calendar year 2001.This patent of invention technology mainly comprises:
A kind of combustion phosphorus tower apparatus that can reclaim heat energy generated during combustion of yellow is provided, and the recovery of heat energy is by means of the many upcasts and the enhanced heat exchange fin thereof that are installed on the combustion phosphorus tower wall.Mainly absorb the heat energy of yellow phosphorus burning by the radiation heat transfer mode;
The using plasma ceramic coating prevents that high temperature phosphorous steam is to the corrosion of metal wall;
A kind of new technology and production system that reclaims heat energy heat production in next life method phosphoric acid of utilizing is provided.At home and abroad, this patent of invention technology be up to now the recovery of heat energy generated during combustion of yellow with utilize the unique case history that succeeds and use in field, and realized industrialization.Yet this technology only provides the combustion phosphorus device (also claiming combustion phosphorus tower) of a kind of single district type, and namely in this combustion phosphorus device, the recovery of heat energy mainly relies on the mode of single radiative transfer.Be that heat energy reclaims be that the high-temperature gas (usually more than 2500 ℃) that produces by means of yellow phosphorus and oxygen reaction and the radiative transfer that fires between the phosphorus device wall are implemented.Theoretical analysis and engineering practice all show: in combustion phosphorus tower, when phosphorus and oxygen generation chemical reaction, except generating the Vanadium Pentoxide in FLAKES of making thermal phosphoric acid, also generate the Tripyrophosphoric acid polymkeric substance, they are super phosphoric acid, metaphosphoric acid, polyphosphoric acid, tetra-sodium, the mixture that ortho-phosphoric acid forms.They accumulate in the conjunctiva layer that has just formed the gas, liquid, solid three-phases on the heat exchanging pipe wall.The conjunctiva aspect to the exospheric temperature of phosphorus combustion flame can be up to 600 ℃ about.Because the existence of this conjunctiva layer, when the temperature of process gas dropped to 700 ℃ of left and right sides, the ability of radiation heat transfer was very little.The temperature out of therefore firing the phosphorus tower all reaches about 700 ℃ usually, that is, the low temperature exhaust heat below 700 ℃ can not effectively be reclaimed.Therefore only rely on radiative transfer mode (that is, the yellow phosphorus phosphoric acid plant of single district type) to implement the recovery of heat energy generated during combustion of yellow, be very restricted.The temperature out of existing (or existing) patent of invention technology is generally 700 ℃, the theoretical recovery of heat energy approximately 65%, and the actual recovered rate is 55-60% approximately.
Summary of the invention
For the deficiency in the background technology, the purpose of this utility model is to provide a kind of device of two-region type high efficiente callback heat energy generated during combustion of yellow, the heat energy recovery rate theoretical value is reached more than 75%, realize thermal phosphoric acid produce in to high efficiente callback and the utilization of yellow phosphorus phosphoric acid heat energy.
The technical solution adopted in the utility model is:
Whole device of the present utility model comprises support, abundant combustion zone assembly, transmission of heat by convection area assembly and drum from bottom to up successively; Fully an end of combustion zone downtake is communicated with drum, and fully the other end of combustion zone downtake is communicated with the lower collecting box of abundant combustion zone assembly; Fully an end of combustion zone water vapor steam guiding tube is communicated with drum, and fully the other end of combustion zone water vapor steam guiding tube is communicated with the upper header of abundant combustion zone assembly; One end of transmission of heat by convection district downtake is communicated with drum, the other end of transmission of heat by convection district downtake is managed with the cooling water inlet in the transmission of heat by convection area assembly and is communicated with, one end of transmission of heat by convection district water vapor steam guiding tube is communicated with drum, the other end of transmission of heat by convection district water vapor steam guiding tube is communicated with steam outlet pipe in the transmission of heat by convection area assembly, and fully the lower cover of combustion zone assembly is connected with support.
Described abundant combustion zone assembly comprises: membrane heat exchanger, phosphorus burner, abundant combustion zone water vapor steam guiding tube, abundant combustion zone downtake, lower cover and phosphorus burner cools water tank; Membrane heat exchanger comprises one group of many upcast, be connected with the enhanced heat exchange fin between one group of many upcast, the two ends of one group of many upcast equidistantly are communicated with the upper header of annular and the lower collecting box of annular respectively, fully an end of combustion zone water vapor steam guiding tube is connected with upper header, fully an end of combustion zone downtake is communicated with lower collecting box, the outside wall surface of membrane heat exchanger is surrounded by lagging material, the phosphorus burner is installed on the bottom wall of membrane heat exchanger, the outside of phosphorus burner is provided with phosphorus burner cools water tank, and the lower cover of lower collecting box lower end is connected with support;
Described transmission of heat by convection area assembly comprises: tube bundle heat exchanger, transmission of heat by convection district water vapor steam guiding tube, transmission of heat by convection district downtake and Vanadium Pentoxide in FLAKES outlet pipe; Tube bundle heat exchanger comprises many upcasts of another group, the two ends of many upcasts of another group are communicated with upper tubesheet and lower tubesheet respectively, one end of transmission of heat by convection district water vapor steam guiding tube is connected with the steam outlet pipe of tube bundle heat exchanger upper end, one end of transmission of heat by convection district downtake is connected with the cooling water inlet pipe of tube bundle heat exchanger lower end, the outside wall surface of tube bundle heat exchanger is surrounded by lagging material, and the Vanadium Pentoxide in FLAKES outlet pipe is installed on the upper cover on upper tubesheet top.
Described drum is provided with steam outlet pipe, the moisturizing inlet pipe, and fully the other end of combustion zone water vapor steam guiding tube, abundant combustion zone downtake, transmission of heat by convection district water vapor steam guiding tube and transmission of heat by convection district downtake is communicated with drum respectively.
Compare with background technology, the beneficial effect that the utlity model has is:
The utility model by in Two Areas (fully combustion zone and transmission of heat by convection district) to the recovery of heat energy generated during combustion of yellow, not only improved the organic efficiency of heat energy; But also the temperature out that can make combustion phosphorus tower is down to below 400 ℃ from present 700 ℃, thereby alleviate in the follow-up aquation technique the further requirement of cooling of Vanadium Pentoxide in FLAKES process gas, reduce the energy consumption that to pay for cool process gas institute in the subsequent technique, further energy-saving and cost-reducing, improve efficiency of energy utilization, and reduce production costs.
The utility model can be realized the high efficiente callback to heat energy generated during combustion of yellow, and theoretical recovery can reach
75%It is above,, the actual recovered rate is brought up to 66-71%, promotes the energy-saving and emission-reduction that thermal phosphoric acid is produced, and further improves efficiency of energy utilization.Reach save energy, economize on resources, purpose with protection of the environment reduces production costs.In the production of thermal phosphoric acid, have broad application prospects.
Description of drawings
Fig. 1 is the total schematic diagram of apparatus structure of two-region type high efficiente callback heat energy generated during combustion of yellow.
Fig. 2 is abundant combustion zone unit construction schematic diagram.
Fig. 3 is the A-A schematic cross-section of Fig. 2.
Fig. 4 is transmission of heat by convection area assembly structural representation.
Fig. 5 is the B-B schematic cross-section of Fig. 4.
Among the figure: 1, abundant combustion zone assembly, 2, the transmission of heat by convection area assembly, 3, drum, 4, support, 11, membrane heat exchanger, 12, the phosphorus burner, 13, abundant combustion zone water vapor steam guiding tube, 14, abundant combustion zone downtake, 15, lower cover, 16, phosphorus burner cools water tank, 21, tube bundle heat exchanger, 22, transmission of heat by convection district water vapor steam guiding tube, 23, transmission of heat by convection district downtake, 24, the Vanadium Pentoxide in FLAKES outlet pipe, 111, abundant combustion zone upcast, 112, the enhanced heat exchange fin, 113, upper header, 114, lower collecting box, 115, lagging material, 211, transmission of heat by convection district upcast, 212, upper tubesheet, 213, lower tubesheet, 214, upper cover, 215, the cooling water inlet pipe, 216, the steam outlet pipe, 217, lagging material, 31, steam outlet pipe, 32, the moisturizing inlet pipe.
Embodiment
The utility model is described in further detail below in conjunction with drawings and Examples.
As shown in Figure 1, whole device of the present utility model comprises support 4, abundant combustion zone assembly 1, transmission of heat by convection area assembly 2 and drum 3 from bottom to up successively; Fully an end of combustion zone downtake 14 is communicated with drum 3, and fully the other end of combustion zone downtake 14 is communicated with the lower collecting box 114 of abundant combustion zone assembly 1; Fully an end of combustion zone water vapor steam guiding tube 13 is communicated with drum 3, and fully the other end of combustion zone water vapor steam guiding tube 13 is communicated with the upper header 113 of abundant combustion zone assembly 1; One end of transmission of heat by convection district downtake 23 is communicated with drum 3, the other end of transmission of heat by convection district downtake 23 is managed 215 with the cooling water inlet in the transmission of heat by convection area assembly 2 and is communicated with, one end of transmission of heat by convection district water vapor steam guiding tube 22 is communicated with drum 3, the other end of transmission of heat by convection district water vapor steam guiding tube 22 is communicated with steam outlet pipe 216 in the transmission of heat by convection area assembly 2, and fully the lower cover 15 of combustion zone assembly 1 is connected with support 4.
Such as Fig. 2, shown in Figure 3, described abundant combustion zone assembly 1 comprises: membrane heat exchanger 11, phosphorus burner 12, abundant combustion zone water vapor steam guiding tube 13, abundant combustion zone downtake 14, lower cover 15 and phosphorus burner cools water tank 16; Membrane heat exchanger 11 comprises one group of many upcast 111, be connected with enhanced heat exchange fin 112 between one group of many upcast 111, the two ends of one group of many upcast 111 equidistantly are communicated with the upper header 113 of annular and the lower collecting box 114 of annular respectively, fully combustion zone water vapor steam guiding tube 13(is more than one, can equidistantly or not be equally spaced) an end be connected with upper header 113, fully combustion zone downtake 14(is more than one, can equidistantly or not be equally spaced) an end be communicated with lower collecting box 114, the outside wall surface of membrane heat exchanger 11 is surrounded by lagging material 115, phosphorus burner 12 is installed on the bottom wall of membrane heat exchanger 11, the outside of phosphorus burner 12 is provided with phosphorus burner cools water tank 16, and the lower cover 15 of lower collecting box 114 lower ends is connected with support 4.
Such as Fig. 4, shown in Figure 5, described transmission of heat by convection area assembly 2 comprises: tube bundle heat exchanger 21, transmission of heat by convection district water vapor steam guiding tube 22, transmission of heat by convection district downtake 23 and Vanadium Pentoxide in FLAKES outlet pipe 24; Tube bundle heat exchanger 21 comprises many upcasts 211 of another group, the two ends of many upcasts 211 of another group are communicated with upper tubesheet 212 and lower tubesheet 213 respectively, transmission of heat by convection district water vapor steam guiding tube 22(is more than one, can equidistantly or not be equally spaced) an end be connected with the steam outlet pipe 216 of tube bundle heat exchanger 21 upper ends, transmission of heat by convection district downtake 23(is more than one, can equidistantly or not be equally spaced) the cooling water inlet pipe 215 of an end and tube bundle heat exchanger 21 lower ends be connected, the outside wall surface of tube bundle heat exchanger 21 is surrounded by lagging material 217, and Vanadium Pentoxide in FLAKES outlet pipe 24 is installed on the upper cover 214 on upper tubesheet 212 tops.
Described drum 3 is provided with steam outlet pipe 31, moisturizing inlet pipe 32, and fully the other end of combustion zone water vapor steam guiding tube 13, abundant combustion zone downtake 14, transmission of heat by convection district water vapor steam guiding tube 22 and transmission of heat by convection district downtake 23 is communicated with drum 3 respectively.
Principle of work of the present utility model:
Employing the utility model can be implemented the high efficiente callback to heat energy generated during combustion of yellow, and its ultimate principle is as follows.For producing the combustion phosphorus tower of 30,000 tons of thermal phosphoric acids per year, its combustion phosphorus amount hourly is 1200 kilograms for industrial scale.The total heat that per hour discharges is about and is roughly equal to 28.62X10
6Joule.As shown in Figure 1, reclaiming heat energy carries out in following Two Areas respectively.That is, abundant assembly 1(the first district, combustion zone) with transmission of heat by convection area assembly 2(Second Region).In abundant combustion zone assembly 1, behind the yellow phosphorus burning, the theoretical temperatures of the process gas of generation is about about 2500 ℃.In abundant combustion zone, by means of the radiation heat transfer mode of membrane heat exchanger 11, reclaim heat energy.But because the surface temperature of heat exchange wall conjunctiva layer is about 600 ℃, the drop in temperature that causes this abundant combustion zone process gas when energy recovery is during to about 700 ℃ of left and right sides, and Radiant exothermicity is very faint.Therefore, in abundant combustion zone, the heat energy of recovery per hour can reach approximately 18.57X10
6Joule.Along with about 700 ℃ process gass enter the transmission of heat by convection district from the abundant combustion zone of firing the phosphorus tower, the recovery of heat energy has changed heat exchange mode, and in the transmission of heat by convection district, the recovery of heat energy is mainly by means of the transmission of heat by convection mode.Convective heat exchange in this transmission of heat by convection zone by pipe bundle heat exchanger 21 can make the temperature of process gas drop to (that is, the temperature out of combustion phosphorus tower also is to enter next technical process, and process gas enters the temperature of hydrated tower) about 400 ℃ from 700 ℃.Thereby, can further reclaim approximately 3.09X10 of heat energy in the transmission of heat by convection district
6Joule.Recovery by heat energy in Two Areas.Total energy recovery amount can reach per hour 21.66X10
6Joule.Theoretical recovery is about 75.7%.5% thermal losses in the deduction engineering practice, the actual recovered rate is about 71.7%, and the theoretical recovery of prior art is about 64.9%.5% thermal losses in the deduction engineering practice, the actual recovered rate is about 59.9%, and the two is compared, and the rate of recovery increases approximately 11.8 percentage points.Therefore, the utility model has been realized the high efficiente callback to waste heat.The below is described in further detail the principle that reclaims heat energy in two different zones respectively.
Principle to high temperature (more than 700 ℃) energy recovery in abundant combustion zone is as follows: such as Fig. 2, shown in Figure 3.Liquid elemental phosphorous and combustion-supporting air under compressed-air actuated effect, spontaneous combustion in phosphorus spray gun enters abundant combustion zone automatically.By the chemical reaction of phosphorus and oxygen, when generating Vanadium Pentoxide in FLAKES, discharge a large amount of heat energy.In this abundant combustion zone, the recovery dependence membrane heat exchanger of heat energy generated during combustion of yellow is implemented.Membrane heat exchanger belongs to the recuperative heat exchanger in the interchanger classification.Utilize the both sides of abundant combustion zone upcast 111 tube walls, will carry out the cold of heat exchange, hot-fluid is divided into two fluid-spaces.Abundant combustion zone upcast 111 wherein, upper header 113, the inside of lower collecting box 114 has formed the fluid-space of cold fluid (that is, reclaiming the working medium of heat energy, water commonly used, steam water interface); And formed the fluid-space of hot-fluid (that is, yellow phosphorus burning reaction generate the process fluids such as Vanadium Pentoxide in FLAKES) by the annular space that abundant combustion zone upcast 111 and enhanced heat exchange fin 112 surround jointly.Utilize the both sides of abundant combustion zone upcast 111 tube walls and enhanced heat exchange fin 112 to carry out cold, the thermal exchange between the hot-fluid.Because in abundant combustion zone, the velocity of flow of process gas is very little, and temperature is very high, thereby heat energy is mainly absorbed by the water in the abundant combustion zone upcast 111 by the mode of radiation heat transfer.Fully the water in the upcast of combustion zone is vaporized because absorbing heat, forms the two-phase fluid of steam-water mixing.Its density is less than the water-mass density of the abundant combustion zone downtake 14 that is positioned at same level.Thereby, produced a motivating force that makes the water natural circulation at the density difference that fully exists between combustion zone downtake 14 and the abundant combustion zone upcast 111.It drives water and carry out natural water circulation between drum 3-abundant combustion zone downtake 14-lower collecting box 114-abundant combustion zone upcast 111-upper header 113-abundant combustion zone water vapor steam guiding tube 13-drum 3.Like this, the water vapors that fully vaporization produces because water is heated in the combustion zone upcast 111 are through upper header 113, fully combustion zone steam guiding tube 13 enters drum 3, at the drum 3 interior water vapors that after carbonated drink is separated, produce from steam outlet pipe 31 outputs.In the water vapor output procedure, in order to ensure fully in the combustion zone upcast 111 sufficient water being arranged, replenish water at low temperature to drum from the moisturizing inlet pipe 32 of drum 3, these water are through abundant combustion zone downtake 14, and lower collecting box 114 flows into abundant combustion zone upcast 111.Thereby in the recovery of abundant combustion zone assembly 1 interior realization to high temperature (more than 700 ℃) process gas heat energy.
As follows in transmission of heat by convection area assembly 2 interior principles to low temperature (below 700 ℃) energy recovery: such as Fig. 4, shown in Figure 5.Yellow phosphorus is after fully burning, and the process gas of generation is along with the recovery of heat energy, and temperature progressively reduces, and when temperature was down to 700 ℃ of left and right sides, because there is the conjunctiva layer in heat exchange surface, its temperature was usually about 600 temperature.Therefore the radiation heat transfer of process gas in membrane heat exchanger is very faint.At this moment, process gas enters the transmission of heat by convection district from abundant combustion zone.In this zone, the recovery dependence pipe bundle heat exchanger of process gas heat energy is implemented.Pipe bundle heat exchanger 21 also belongs to the recuperative heat exchanger in the interchanger classification.Utilize the both sides of transmission of heat by convection district upcast 211 tube walls, will carry out the cold of heat exchange, hot-fluid is divided into two fluid-spaces.Wherein, the inside of transmission of heat by convection district upcast 211 has formed the fluid-space of hot-fluid (that is, the process fluids such as Vanadium Pentoxide in FLAKES of yellow phosphorus burning reaction generation); And by the outside and the upper tubesheet 212 of transmission of heat by convection district upcast 211, the space of (being between the tube bank of upcast) then forms the fluid-space of cold fluid (that is, reclaiming the working medium of heat energy, water commonly used, steam water interface) between the lower tubesheet 213.Utilize the both sides of transmission of heat by convection district upcast 211 tube walls to carry out cold, the thermal exchange between the hot-fluid.Because in this zone, not only heat interchanging area can increase, and process gas also is greatly improved in interbank velocity of flow.The rapid flow of process gas has not only effectively increased process gas and has reclaimed heat energy working medium (namely, water) convection heat transfer intensity between, and, because flow of process gases washing away upcast inboard, transmission of heat by convection district, cause gas phase conjunctiva layer to flow the attenuation of liquid phase conjunctiva layer with process gas.Be unfavorable for that gas phase and liquid phase conjunctiva thing are in the generation of heat exchange surface.Its result drops to below 350 ℃ the surface temperature of conjunctiva layer.Thereby in the transmission of heat by convection district, the water between heat energy is mainly restrained by upcast by the mode of convective heat exchange absorbs.Water is vaporized because absorbing heat, forms the two-phase fluid of steam-water mixing.Its density is less than the water-mass density of the transmission of heat by convection district downtake 23 that is positioned at same level.Thereby the density difference that water exists between transmission of heat by convection district downtake 23 and 211 tube banks of transmission of heat by convection district upcast has produced a motivating force that makes the water natural circulation.Its drive water between the tube bank of pipe 215-transmission of heat by convection district, downtake 23-cooling water inlet, drum 3-transmission of heat by convection district upcast 211-carry out natural water circulation between steam outlet pipe 216-transmission of heat by convection district water vapor steam guiding tube 22-drum 3.Like this, the water between transmission of heat by convection district upcast is restrained is exported from steam outlet pipe 31 at the drum 3 interior water vapors that produce after carbonated drink is separated because the water vapor that the vaporization of being heated produces enters drum 3 through steam outlet pipe 216, water vapor steam guiding tube 22.In the water vapor output procedure, between the tube bank in order to ensure transmission of heat by convection district upcast 211 sufficient water is arranged, from the moisturizing inlet pipe 32 of drum 3, replenish water at low temperature to drum, these water are through transmission of heat by convection district downtake 23, and cooling water inlet pipe 215 flows between the tube bank of transmission of heat by convection district upcast 211.Thereby strengthening the recovery of convective heat exchange area assembly 2 interior realizations to low temperature (below 700 ℃) process gas heat energy.
Claims (4)
1. the device of a two-region type high efficiente callback heat energy generated during combustion of yellow is characterized in that: whole device comprises support (4), fully combustion zone assembly (1), transmission of heat by convection area assembly (2) and drum (3) from bottom to up successively;
Fully an end of combustion zone downtake (14) is communicated with drum (3), and fully the other end of combustion zone downtake (14) is communicated with the lower collecting box (114) of abundant combustion zone assembly (1); Fully an end of combustion zone water vapor steam guiding tube (13) is communicated with drum (3), and fully the other end of combustion zone water vapor steam guiding tube (13) is communicated with the upper header (113) of abundant combustion zone assembly (1); One end of transmission of heat by convection district downtake (23) is communicated with drum (3), the other end of transmission of heat by convection district downtake (23) is managed (215) with the cooling water inlet in the transmission of heat by convection area assembly (2) and is communicated with, one end of transmission of heat by convection district water vapor steam guiding tube (22) is communicated with drum (3), the other end of transmission of heat by convection district water vapor steam guiding tube (22) is communicated with steam outlet pipe (216) in the transmission of heat by convection area assembly (2), and fully the lower cover (15) of combustion zone assembly (1) is connected with support (4).
2. the device of a kind of two-region type high efficiente callback heat energy generated during combustion of yellow according to claim 1, it is characterized in that: described abundant combustion zone assembly (1) comprising: membrane heat exchanger (11), phosphorus burner (12), fully combustion zone water vapor steam guiding tube (13), fully combustion zone downtake (14), lower cover (15) and phosphorus burner cools water tank (16); Membrane heat exchanger (11) comprises one group of many upcast (111), be connected with enhanced heat exchange fin (112) between one group of many upcast (111), the two ends of one group of many upcast (111) equidistantly are communicated with the upper header (113) of annular and the lower collecting box (114) of annular respectively, fully an end of combustion zone water vapor steam guiding tube (13) is connected with upper header (113), fully an end of combustion zone downtake (14) is communicated with lower collecting box (114), the outside wall surface of membrane heat exchanger (11) is surrounded by lagging material (115), phosphorus burner (12) is installed on the bottom wall of membrane heat exchanger (11), the outside of phosphorus burner (12) is provided with phosphorus burner cools water tank (16), and the lower cover (15) of lower collecting box (114) lower end is connected with support (4).
3. the device of a kind of two-region type high efficiente callback heat energy generated during combustion of yellow according to claim 1, it is characterized in that: described transmission of heat by convection area assembly (2) comprising: tube bundle heat exchanger (21), transmission of heat by convection district water vapor steam guiding tube (22), transmission of heat by convection district downtake (23) and Vanadium Pentoxide in FLAKES outlet pipe (24); Tube bundle heat exchanger (21) comprises another group many upcasts (211), the two ends of another many upcasts of group (211) are communicated with upper tubesheet (212) and lower tubesheet (213) respectively, one end of transmission of heat by convection district water vapor steam guiding tube (22) is connected with the steam outlet pipe (216) of tube bundle heat exchanger (21) upper end, one end of transmission of heat by convection district downtake (23) is connected with the cooling water inlet pipe (215) of tube bundle heat exchanger (21) lower end, the outside wall surface of tube bundle heat exchanger (21) is surrounded by lagging material (217), and Vanadium Pentoxide in FLAKES outlet pipe (24) is installed on the upper cover (214) on upper tubesheet (212) top.
4. the device of a kind of two-region type high efficiente callback heat energy generated during combustion of yellow according to claim 1, it is characterized in that: described drum (3) is provided with steam outlet pipe (31), moisturizing inlet pipe (32), fully the other end of combustion zone water vapor steam guiding tube (13), abundant combustion zone downtake (14), transmission of heat by convection district water vapor steam guiding tube (22) and transmission of heat by convection district downtake (23) is communicated with drum (3) respectively.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201220554682 CN202864923U (en) | 2012-10-26 | 2012-10-26 | Double-zone efficient device for recovering yellow phosphorus combustion heat energy |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201220554682 CN202864923U (en) | 2012-10-26 | 2012-10-26 | Double-zone efficient device for recovering yellow phosphorus combustion heat energy |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN202864923U true CN202864923U (en) | 2013-04-10 |
Family
ID=48031661
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 201220554682 Withdrawn - After Issue CN202864923U (en) | 2012-10-26 | 2012-10-26 | Double-zone efficient device for recovering yellow phosphorus combustion heat energy |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN202864923U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102910602A (en) * | 2012-10-26 | 2013-02-06 | 浙江诚泰化工机械有限公司 | Double-region device for efficiently recovering yellow phosphorus combustion heat |
| CN103738930A (en) * | 2013-12-27 | 2014-04-23 | 成都易态科技有限公司 | Method and device for producing yellow phosphorus by using large self baking electrode phosphorus producing electric furnace |
-
2012
- 2012-10-26 CN CN 201220554682 patent/CN202864923U/en not_active Withdrawn - After Issue
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102910602A (en) * | 2012-10-26 | 2013-02-06 | 浙江诚泰化工机械有限公司 | Double-region device for efficiently recovering yellow phosphorus combustion heat |
| CN103738930A (en) * | 2013-12-27 | 2014-04-23 | 成都易态科技有限公司 | Method and device for producing yellow phosphorus by using large self baking electrode phosphorus producing electric furnace |
| CN103738930B (en) * | 2013-12-27 | 2016-06-15 | 成都易态科技有限公司 | Large-scale self baking electrode phosphor furnace is used to produce method and the equipment of yellow phosphorus |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN102517065B (en) | Self-heating type biomass fast pyrolysis liquefying device | |
| CN102910602B (en) | Double-region device for efficiently recovering yellow phosphorus combustion heat | |
| CN201942519U (en) | Thermal energy recovery and utilization device in production of thermal phosphoric acid and production system of thermal energy recovery and utilization device | |
| CN101571280B (en) | Multi-pressure and multi-inlet generating waste heat boiler | |
| CN102815679B (en) | Special phosphorus burning tower and thermal-process phosphoric acid production heat-electricity self-balancing system | |
| CN102925165A (en) | Afterheat recovery system for raw coke oven gas of coke oven ascension pipe | |
| CN201485272U (en) | Pipe casing type waste heat boiler system equipment of sulfur recovery unit | |
| CN203068991U (en) | Combined waste heat utilization heat pipe waste heat boiler | |
| CN202864923U (en) | Double-zone efficient device for recovering yellow phosphorus combustion heat energy | |
| CN111336487A (en) | Coke oven raw gas and waste gas waste heat recycling system | |
| CN107166358B (en) | Boiler system for producing double heat carriers | |
| CN106123632B (en) | A kind of method to be generated electricity using residual heat of aluminum reduction cell | |
| CN202430008U (en) | Device for phosphorus pentoxide production and thermal energy recovery | |
| CN202440467U (en) | Self-heating biomass flash pyrolysis liquefying device | |
| CN202766296U (en) | Special phosphoric acid tower and self-balancing system for producing phosphoric acids by hot method | |
| CN211822292U (en) | Coke oven raw gas and waste gas waste heat recycling system | |
| CN202947112U (en) | Low-grade double-effect phase-change waste heat recovery system for recycling of waste gas and waste heat | |
| CN108131656B (en) | Ultra-clean emission cold and hot co-production system of coking plant | |
| CN102556990B (en) | Device for absorbing heat energy from combustion of yellow phosphorus with heat transfer oil | |
| CN203486905U (en) | Hot-process phosphoric acid waste-heat utilizing device with radiation convective heat transfer surface | |
| CN202993141U (en) | Distributed waste heat boiler based on carbon plant calcining furnace calcined coke attached heat pipe heat exchange | |
| CN103471421B (en) | Device for recovering waste heat of high-temperature flue and exhaust heat recovering method thereof | |
| CN208982184U (en) | A kind of tedge waste heat Stirling electricity generation system | |
| CN203177678U (en) | Waste heat recovery system based on tunnel kiln and waste heat power generation system comprising same | |
| CN202057214U (en) | Pipe heat exchanger by utilizing residual heat of thermal phosphoric acid device to produce inorganic salt |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| AV01 | Patent right actively abandoned |
Granted publication date: 20130410 Effective date of abandoning: 20140430 |
|
| RGAV | Abandon patent right to avoid regrant |