CN204752207U - Utilize dry waste heat heating sulfur trioxide's of sodium hydrosulfite energy -conserving heating device - Google Patents
Utilize dry waste heat heating sulfur trioxide's of sodium hydrosulfite energy -conserving heating device Download PDFInfo
- Publication number
- CN204752207U CN204752207U CN201520379007.9U CN201520379007U CN204752207U CN 204752207 U CN204752207 U CN 204752207U CN 201520379007 U CN201520379007 U CN 201520379007U CN 204752207 U CN204752207 U CN 204752207U
- Authority
- CN
- China
- Prior art keywords
- drying chamber
- water back
- anger
- air inlet
- sodium hydrosulfite
- 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.)
- Active
Links
Classifications
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/10—Process efficiency
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/10—Process efficiency
- Y02P20/129—Energy recovery, e.g. by cogeneration, H2recovery or pressure recovery turbines
Landscapes
- Thermotherapy And Cooling Therapy Devices (AREA)
- Drying Of Solid Materials (AREA)
Abstract
The utility model discloses an utilize dry waste heat heating sulfur trioxide's of sodium hydrosulfite energy -conserving heating device, including the drying chamber and the jar that admits air, the lower part of drying chamber is equipped with the support frame, is equipped with the interface that admits air on the drying chamber, the interface of giving vent to anger, pan feeding lid, ejection of compact lid, motor, (mixing) shaft and a pair of stirring leaf, installs a set of electrothermal tube component that is used for the heat drying sodium hydrosulfite on this drying chamber inner wall, is equipped with pressure connection on the jar that admits air, and a U type water back is installed to the articulate of giving vent to anger of jar lower part of should admitting air, and screw set has the spiral curved tube on the outer wall of U type water back. The utility model discloses send the steam of the high fever of sodium hydrosulfite heat drying evaporation into the spiral curved tube, through the heat exchange with the inside sulfur trioxide heating of U type water back, practiced thrift a large amount of energy for the processing of sodium hydrosulfite, has improved energy utilization greatly and has rateed.
Description
Technical field
The utility model relates to a kind of energy-saving heating apparatus utilizing the dry waste-heat sulphur trioxide of vat powder.
Background technology
At present, in the processing of vat powder (V-Brite B), need to use sulphur trioxide to carry out oxidation and sulfidizing synthesis, and needed first to carry out heat treated to sulphur trioxide before oxidation and sulfidizing, traditional method is, direct use electric heating device carries out heat treated to sulphur trioxide, needs the energy of at substantial like this.
Further, vat powder is when producing, often need to carry out heat drying process to finished product vat powder, during heat drying process, by the aqueous vapor evaporation in vat powder, the aqueous vapor temperature evaporated is very high, there is a large amount of heats, and conventional art is by direct for the steam of this part exhausted air, what which results in the energy utilizes rate variance, a large amount of wasting of resources caused.
Utility model content
The utility model, in order to solve the above-mentioned deficiency of prior art, proposes a kind of energy-saving heating apparatus utilizing the dry waste-heat sulphur trioxide of vat powder.
In order to solve the problems of the technologies described above, the utility model is by the following technical solutions: a kind of energy-saving heating apparatus utilizing the dry waste-heat sulphur trioxide of vat powder, comprise drying chamber and air inlet tank, the bottom of described drying chamber is provided with bracing frame, the upper end of drying chamber is respectively equipped with intake interface and interface of giving vent to anger, the side of drying chamber is provided with the pan feeding lid of the powder that takes a policy, the downside of drying chamber is provided with discharging lid, and the top of this drying chamber is provided with motor, the output shaft of described motor is connected to the stir shaft be placed in drying chamber, described stir shaft is provided with a pair paddle, this drying chamber inwall is provided with one group of electrical heating tube element for heat drying vat powder.
The upper end of described air inlet tank is provided with the inlet suction port of sulphur trioxide, the air outlet adapter of this air inlet tank bottom is connected and installed with a U-shaped water back, on the outer wall of described U-shaped water back, spiral is provided with spiral curved tube, the two ends of U-shaped water back are respectively air inlet termination and termination of giving vent to anger, described air inlet termination is connected with the air outlet adapter of air inlet tank bottom, the two ends of described spiral curved tube are respectively equipped with hot gas inlet pipe and hot gas goes out pipe, to give vent to anger described in described hot gas inlet pipe is connected to interface, and hot gas inlet pipe is arranged on the termination homonymy of giving vent to anger of U-shaped water back.
Compared with prior art, the utility model is with the heat drying structure of vat powder, when drying, in drying chamber, electrical heating tube element is not only by vat powder heat drying, also by the aqueous vapor evaporation in vat powder, the steam temperature of the evaporation of this part is very high, the steam of high heat enters into spiral curved tube, by heat exchange, the sulphur trioxide of U-shaped water back inside is heated, and the flow direction of hot steam is contrary with the flow direction of sulphur trioxide, greatly increase heat exchange efficiency, a large amount of energy has been saved in processing for vat powder, improve the utilization ratio of the energy, and total is simple, be easy to realize, be worthy to be popularized.
Accompanying drawing explanation
Fig. 1 is structural representation of the present utility model.
Embodiment
Below in conjunction with drawings and Examples, utility model is described in detail.
As shown in Figure 1, the energy-saving heating apparatus utilizing the dry waste-heat sulphur trioxide of vat powder that the utility model proposes, comprise drying chamber 1 and air inlet tank 2, the bottom of drying chamber is provided with bracing frame 3, the upper end of drying chamber 1 is respectively equipped with intake interface 4 and interface 5 of giving vent to anger, the side of drying chamber is provided with the pan feeding lid 6 of the powder that takes a policy, the downside of drying chamber is provided with discharging lid 7, and the top of this drying chamber is provided with motor 8, the output shaft of motor 8 is connected to the stir shaft 9 be placed in drying chamber, stir shaft is provided with a pair paddle 10, this drying chamber inwall is provided with one group of electrical heating tube element 11 for heat drying vat powder.
The upper end of air inlet tank 2 is provided with the inlet suction port 12 of sulphur trioxide, the air outlet adapter 13 of this air inlet tank 2 bottom is connected and installed with a U-shaped water back 14, on the outer wall of U-shaped water back 14, spiral is provided with spiral curved tube 15, the two ends of U-shaped water back 14 are respectively air inlet termination 16 and termination 17 of giving vent to anger, air inlet termination 16 is connected with the air outlet adapter 13 of air inlet tank 2 bottom, the two ends of spiral curved tube 15 are respectively equipped with hot gas inlet pipe 18 and hot gas goes out pipe 19, hot gas inlet pipe 18 is connected to interface 5 of giving vent to anger, and hot gas inlet pipe 18 is arranged on termination 17 homonymy of giving vent to anger of U-shaped water back 13.
The operation of the heat drying operation of vat powder and the heat temperature raising of sulphur trioxide combines by the utility model, the waste heat of the hot steam utilizing the heat drying of vat powder to produce fully, uses waste heat to carry out intensification heating to sulphur trioxide.Wherein, when carrying out the heat drying of vat powder, wet vat powder is put in drying chamber, electrical heating tube element 11 connects power work, heating vat powder, and motor 8 also works, and drives stir shaft 9 to rotate, the direction of rotating is positive and negative two-way, it is even that vat powder just can be stirred heat exchange by the paddle on such stir shaft, and now, the dry hot steam produced flows out from interface 5 of giving vent to anger, flow in hot gas inlet pipe 18, flow out going out pipe 19 from hot gas.The sulphur trioxide do not heated is poured in the top of air inlet tank 2, sulphur trioxide enters from the air inlet termination 16 of U-shaped water back 14, flow out from termination 17 of giving vent to anger again, and flowing through in process, the sulphur trioxide of U-shaped water back inside is heated by heat exchange at helical curve Bottomhole pressure by the hot steam of high heat, and the flow direction of the flow direction of hot steam and sulphur trioxide is contrary, greatly increase heat exchange efficiency, a large amount of energy has been saved in the processing for vat powder.
Above-described embodiment only have expressed several embodiment of the present utility model, and it describes comparatively concrete and detailed, but therefore can not be interpreted as the restriction to the utility model the scope of the claims.It should be pointed out that for the person of ordinary skill of the art, without departing from the concept of the premise utility, can also make some distortion and improvement, these all belong to protection domain of the present utility model.Therefore, the utility model patent and protection domain should be as the criterion with appended claims.
Claims (1)
1. one kind utilizes the energy-saving heating apparatus of the dry waste-heat sulphur trioxide of vat powder, it is characterized in that: comprise drying chamber (1) and air inlet tank (2), the bottom of described drying chamber is provided with bracing frame (3), the upper end of drying chamber (1) is respectively equipped with intake interface (4) and interface of giving vent to anger (5), the side of drying chamber is provided with the pan feeding lid (6) of the powder that takes a policy, the downside of drying chamber is provided with discharging lid (7), and the top of this drying chamber is provided with motor (8), the output shaft of described motor (8) is connected to the stir shaft (9) be placed in drying chamber, described stir shaft is provided with a pair paddle (10), this drying chamber inwall is provided with one group of electrical heating tube element for heat drying vat powder (11),
The upper end of described air inlet tank (2) is provided with the inlet suction port (12) of sulphur trioxide, the air outlet adapter (13) of this air inlet tank (2) bottom is connected and installed with a U-shaped water back (14), on the outer wall of described U-shaped water back (14), spiral is provided with spiral curved tube (15), the two ends of U-shaped water back (14) are respectively air inlet termination (16) and termination of giving vent to anger (17), described air inlet termination (16) is connected with the air outlet adapter (13) of air inlet tank (2) bottom, the two ends of described spiral curved tube (15) are respectively equipped with hot gas inlet pipe (18) and hot gas goes out pipe (19), to give vent to anger described in described hot gas inlet pipe (18) is connected to interface (5), and hot gas inlet pipe (18) is arranged on termination of giving vent to anger (17) homonymy of U-shaped water back (13).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520379007.9U CN204752207U (en) | 2015-06-05 | 2015-06-05 | Utilize dry waste heat heating sulfur trioxide's of sodium hydrosulfite energy -conserving heating device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520379007.9U CN204752207U (en) | 2015-06-05 | 2015-06-05 | Utilize dry waste heat heating sulfur trioxide's of sodium hydrosulfite energy -conserving heating device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN204752207U true CN204752207U (en) | 2015-11-11 |
Family
ID=54466936
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201520379007.9U Active CN204752207U (en) | 2015-06-05 | 2015-06-05 | Utilize dry waste heat heating sulfur trioxide's of sodium hydrosulfite energy -conserving heating device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN204752207U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107751117A (en) * | 2017-11-23 | 2018-03-06 | 广州飞禧特生物科技有限公司 | Black soldier flies larva separates drying equipment and method |
| CN107787925A (en) * | 2017-11-23 | 2018-03-13 | 广州飞禧特生物科技有限公司 | Black soldier flies larva cultivation separation drying equipment and method |
-
2015
- 2015-06-05 CN CN201520379007.9U patent/CN204752207U/en active Active
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107751117A (en) * | 2017-11-23 | 2018-03-06 | 广州飞禧特生物科技有限公司 | Black soldier flies larva separates drying equipment and method |
| CN107787925A (en) * | 2017-11-23 | 2018-03-13 | 广州飞禧特生物科技有限公司 | Black soldier flies larva cultivation separation drying equipment and method |
| CN107751117B (en) * | 2017-11-23 | 2023-08-11 | 广州飞禧特生物科技有限公司 | Black soldier fly larva separation and drying equipment and method |
| CN107787925B (en) * | 2017-11-23 | 2023-08-11 | 广州飞禧特生物科技有限公司 | Black soldier fly larva breeding, separating and drying equipment and method |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN204752207U (en) | Utilize dry waste heat heating sulfur trioxide's of sodium hydrosulfite energy -conserving heating device | |
| CN210832658U (en) | Circulating water cooling device for construction equipment | |
| CN206382009U (en) | The fast reactor of condensing rate | |
| CN211204756U (en) | Production equipment for quickly drying desulfurized gypsum | |
| CN204727610U (en) | A kind of circulating heater utilizing the dry waste-heat sulphur trioxide of vat powder | |
| CN208898821U (en) | A kind of environmental protection and energy saving coal gas generating device | |
| CN208414199U (en) | Circulating sludge drying device in a kind of vapor | |
| CN206392065U (en) | A kind of Titanium series catalyst preparation facilities | |
| CN207694690U (en) | A kind of bio-feritlizer processing homogenization tank | |
| CN204803247U (en) | Formaldehyde preparation device of methyl alcohol direct boiling | |
| CN210980649U (en) | A drying device for mercuric chloride catalyst production | |
| CN209828980U (en) | A reation kettle for producing flocculating agent | |
| CN202478678U (en) | Flocculation device | |
| CN206450016U (en) | A kind of catalyst drying machine | |
| CN207865946U (en) | Predecomposition rotary kiln residual heat using device | |
| CN207180240U (en) | A kind of preparing protodrug crystal drying system | |
| CN206103912U (en) | Reaction unit of glyoxal oxidation glyoxalic acid | |
| CN220803182U (en) | Closed hydrolysis reactor with adjustable heating rate | |
| CN205975184U (en) | Paper pulp apparatus for producing with waste gas treatment system | |
| CN205062030U (en) | Crude oil of oil chaff granule leaches device | |
| CN215654849U (en) | Waterborne environmental protection emulsion heating device | |
| CN208382761U (en) | A kind of circulation drier of tea-leaf power | |
| CN114485214B (en) | Waste heat recovery device for white carbon black production | |
| CN220689356U (en) | Heat pump with multi-medium mixed heating | |
| CN219567819U (en) | Preheating device for lime production |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant |