CN104819446A - Energy-saving steam regeneration system and method - Google Patents
Energy-saving steam regeneration system and method Download PDFInfo
- Publication number
- CN104819446A CN104819446A CN201510262162.7A CN201510262162A CN104819446A CN 104819446 A CN104819446 A CN 104819446A CN 201510262162 A CN201510262162 A CN 201510262162A CN 104819446 A CN104819446 A CN 104819446A
- Authority
- CN
- China
- Prior art keywords
- steam
- vapor
- water
- liquid separation
- separator
- 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.)
- Granted
Links
Landscapes
- Heat Treatment Of Water, Waste Water Or Sewage (AREA)
- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
Abstract
The invention provides an energy-saving steam regeneration system and method. The system comprises a steam regenerating unit, a water source regenerating unit and a connecting pipe, wherein the steam regenerating unit comprises an evaporator and a steam liquid separating mechanism, the steam inlet of the evaporator communicates with the steam discharge hole of a steam box, the water inlet of the evaporator communicates with the water outlet of the steam and liquid separating mechanism, the steam discharge hole of the evaporator communicates with the steam inlet of the steam and liquid separating mechanism, the steam discharging hole of the steam and liquid separating mechanism communicates with the steam inlet of the steam box, and the water source regenerating unit comprises a first separator. The method comprises the steps of: 1, heat exchange; 2, recycle of high temperature steam and liquid mixed water source; 3, utilization of moisture in high temperature steam. According to the system and the method, the high temperature steam generated by the steam box can be well recycled and reused.
Description
Technical field
The invention belongs to food processing equipment technical field, especially relate to a kind of steam regeneration energy conserving system.
Background technology
At food-processing industry, steam box is the required equipment of food processing line, molded food product is supplied to citizen after steam box cooks, its concrete operations are: be placed on by foods to be processed on the food steamer in steam box, steam box adds thermosetting high-temperature steam by the water that heater is continuously in steam chest, to cooking food in the process risen from lower to upper along with the high-temperature steam in steam box, used steam is discharged in air by steam box floss hole.This food processing mode Problems existing is: the vapor (steam) temperature of discharging through steam box floss hole is generally 95 ° ~ 100 °, and therefore this discharging modes of high-temperature steam cause a large amount of wastes of the energy.
Application number be 201310590336.3 apply for a patent to steam box discharge steam recycle, in this patent, include steam box, heat storage water tank, cyclic water tank and domestic hot-water's terminal, and connecting pipeline and valve, the steam (vapor) outlet of steam box is communicated with the air intake of heat storage water tank, heat storage water tank inside is provided with heat exchanger, the outlet of heat exchanger is communicated with entrance is corresponding with the low-temperature circulating water out that bottom is provided with the high temperature circulation water inlet that cyclic water tank top is provided with respectively, and the high temperature circulation water out that cyclic water tank top is arranged is communicated with domestic hot-water's terminal; Its specific implementation process is, the steam discharged by steam box enters into heat storage water tank, submergence heat exchange is carried out with the water storage in heat storage water tank, now water storage is heated as high-temperature-hot-water, low-temperature water heating in cyclic water tank forms high temperature circulation water after heat exchanger, this high temperature circulation water is transported to cyclic water tank deposit to be domestic water or to be again transported to heat storage water tank and to carry out heat exchange, can also directly supply water supply tank to provide water source to steam box.This application patent achieves the utilization again to steam energy, but its drawback existed is: the steam discharged by steam box carries out the heat exchange method of immersion in heat storage water tank, steam condenses into water after carrying out heat exchange, after water level exceedes the overfall of heat storage water tank, unnecessary water flows out from overfall, water storage now in storage tank is high-temperature water, and these discharging modes cause loss and the waste of water source and thermal source, and therefore the energy recovery of the application's patent is not thorough.
Summary of the invention
In view of this, the present invention is intended to propose a kind of steam regeneration energy conserving system and method, to solve the steam of existing steam box in the art owing to discharging the improper energy waste problem caused.
For achieving the above object, technical scheme of the present invention is achieved in that
A kind of steam regeneration energy conserving system, this system is applied to steam box, described steam regeneration energy conserving system comprises steam regeneration unit, water source regeneration unit and connecting pipe, described steam regeneration unit comprises evaporimeter and vapor-liquid separation mechanism, the air intake that described evaporimeter top is provided with is communicated with the steam outlet of steam box, the water inlet that described base of evaporator is provided with is communicated with the delivery port of vapor-liquid separation mechanism, the steam drain that described evaporimeter top is provided with is communicated with the air intake of vapor-liquid separation mechanism, the steam drain that described vapor-liquid separation mechanism is provided with is communicated with the air intake of steam box, described vapor-liquid separation mechanism is provided with external pipe, vapor-liquid separation mechanism is connected by external pipe and external water source,
Described water source regeneration unit comprises the first separator, and the water inlet of described first separator is connected with the discharge outlet that base of evaporator is provided with, and the regeneration water source water inlet that delivery port and the vapor-liquid separation mechanism of described first separator are provided with is connected.
Further, described vapor-liquid separation mechanism comprises storage tank and the second separator, described second separator is arranged on directly over storage tank, and described second separator is connected with storage tank, ensure that the aqueous water be separated through the second separator flow in storage tank thus, the delivery port of described vapor-liquid separation mechanism, regeneration water source water inlet and external pipe are separately positioned on storage tank, and air intake and the steam drain of described vapor-liquid separation mechanism are arranged on the second separator.
Further, in described storage tank, be provided with liquid level gauge, by the height of water level in liquid level gauge observation storage tank.
Further, at evaporimeter with vapor-liquid separation is inter-agency is provided with the first water pump, described first water pump and vapor-liquid separation is inter-agency is provided with temperature sensor.
Further, described first separator and vapor-liquid separation is inter-agency is provided with the second water pump, described second water pump and vapor-liquid separation is inter-agency is provided with filter, the Impurity removal in the aqueous water that recovered steam is formed by this filter after evaporator falls to be formed pure regeneration water source.
Further, the top of described first separator is provided with air discharge ports, and described air discharge ports is connected with vacuum blower.
Further, described evaporimeter is plate type heat exchanger.
Further, between vapor-liquid separation mechanism and steam box, be provided with roots blower, this roots blower can heat the steam through vapor-liquid separation organizational separation and pressurize before flowing to steam box, and then meets temperature requirement and the pressure requirements of steam box steam used.
A kind of steam regeneration power-economizing method of applying steam regenerating energy-saving system, the steps include:
The high-temperature steam that steam box discharges is transported in evaporimeter, heat exchange is carried out with the water at low temperature inputted by vapor-liquid separation mechanism in evaporimeter, water at low temperature presents the vapour-liquid admixture of high temperature after heat exchange, high-temperature steam condenses into aqueous water simultaneously, after the heat exchange, high-temperature water in vapour-liquid admixture is delivered to vapor-liquid separation mechanism, by vapor-liquid separation mechanism, the vapour-liquid of high temperature mixing water source is carried out vapor-liquid separation, vapor portion in vapour-liquid mixing water source is transported to steam box and utilizes, aqueous water part in vapour-liquid mixing water source is transported to evaporimeter and carries out heat exchange again, complete the recycling of the steam heat discharged by steam box thus, meanwhile, the aqueous water that high-temperature steam condenses after evaporator heat exchange is delivered to vapor-liquid separation mechanism through the first separator, be delivered to evaporimeter through vapor-liquid separation mechanism and carry out heat exchange, and finally flow to steam box in vapour form, complete recovery and utilization that the water from steam that discharged by steam box divides.
Further, utilize roots blower heat before flowing to steam box the steam by vapor-liquid separation organizational separation and pressurize, and then meet steam box to the temperature requirement of steam and pressure requirements.
Relative to prior art, a kind of steam regeneration energy conserving system of the present invention has following advantage:
(1) in a kind of steam regeneration energy conserving system of the present invention, heat carries out exchanging and the high-temperature steam that finally formation is fresh through steam regeneration unit by the high-temperature steam of steam box discharge, this fresh high-temperature steam flows to steam box and utilizes, and therefore achieves the recovery and reuse of heat; In addition, the high-temperature steam of steam box discharge is condensed into aqueous water after heat exchange, this aqueous water is by flowing to vapor-liquid separation mechanism after the first separator in water source regeneration unit, and then enter into steam regeneration unit and again utilize, achieve the recovery and reuse at high-temperature steam water source, this system recoveries rate is high, has saved cost to a great extent, and reduces the loss of the energy.
(2) in a kind of steam regeneration energy conserving system of the present invention, the first water pump and temperature sensor is had between vapor-liquid separation mechanism and evaporated devices, by temperature sensor, temperature detection is carried out to the water at low temperature of being carried to evaporimeter by vapor-liquid separation mechanism, and by signal transmission to control centre, control centre controls the rotating speed of the first water pump, when water temperature is lower, first water pump low-speed running, extend the heat exchanger time of water at low temperature in evaporimeter, improve the heat exchange effect of water at low temperature in evaporimeter, and then ensure that the water source of the vapour-liquid admixture of being carried to vapor-liquid separation mechanism by evaporimeter has higher temperature.
(3) in a kind of steam regeneration energy conserving system of the present invention, at the first separator with vapor-liquid separation is inter-agency is provided with strainer valve, impurity in the aqueous water that high-temperature steam is formed after heat exchange is filtered out by strainer valve, ensure that the cleanliness factor of the steam entered in steam box, namely ensured that the steam flowing to steam box is live steam, and then ensure that the hygienic requirements that steam box is processed food.
(4) in a kind of steam regeneration energy conserving system of the present invention, vacuum blower is connected with in the air discharge ports of the first separator, vacuum blower is on the one hand for the high-temperature steam discharged by steam box provides guiding power, ensure that in evaporimeter, heat exchange is carried out smoothly, on the other hand the air contained in the aqueous water reclaimed by evaporimeter is excluded, avoid when subsequent cycle, the loss of the energy that the air in water causes because of absorption energy.
Relative to prior art, a kind of steam regeneration power-economizing method of the present invention has following advantage:
(1) a kind of steam regeneration power-economizing method of the present invention, in the method, the heat of high-temperature steam to steam box discharge and the recovery and reuse at water source are realized by the step that utilizes of the moisture in the recycling step at the vapour-liquid of heat exchanging step, high temperature mixing water source and high-temperature steam, the method has saved cost to a great extent, reduces the consumption of the energy.
Accompanying drawing explanation
The accompanying drawing forming a part of the present invention is used to provide a further understanding of the present invention, and schematic description and description of the present invention, for explaining the present invention, does not form inappropriate limitation of the present invention.In the accompanying drawings:
Fig. 1 is the structural representation of a kind of steam regeneration energy conserving system described in the embodiment of the present invention;
Description of reference numerals:
1-steam box, 2-first separator, 3-evaporimeter,
4-filter, 5-second separator, 6-storage tank,
7-roots blower, 8-temperature sensor, 9-first water pump,
10-second water pump, 11-vacuum blower, 12-air discharge ports,
13-steam drain.
Detailed description of the invention
It should be noted that, when not conflicting, the embodiment in the present invention and the feature in embodiment can combine mutually.
Below with reference to the accompanying drawings and describe the present invention in detail in conjunction with the embodiments.
As shown in Figure 1, a kind of steam regeneration energy conserving system, this system is applied to steam box 1, described steam regeneration energy conserving system comprises steam regeneration unit, water source regeneration unit and connecting pipe, described steam regeneration unit comprises evaporimeter 3 and vapor-liquid separation mechanism, described vapor-liquid separation mechanism comprises storage tank 6 and the second separator 5, described second separator 5 is arranged on directly over storage tank 6, and the bottom of described second separator 5 is provided with delivery port, water inlet is provided with at the top of storage tank 6, the delivery port of described second separator 5 is communicated with the water inlet of storage tank 6, ensure that the aqueous water be separated through the second separator 5 flow in storage tank 6 stand-by thus, the bottom of described storage tank 6 is provided with delivery port and regeneration water source water inlet, the middle part of described storage tank 6 tank wall is provided with external water source water inlet, this external water source water inlet is communicated with external water source by external pipe, second separator 5 is provided with air intake and steam drain 13, liquid level gauge is provided with in described storage tank 6, by the height of water level in liquid level gauge observation storage tank 6, and supply water to storage tank 6 in time according to observed result or stop supplying water, in the present embodiment, liquid level detecting sensor selected by liquid level gauge 6, and the control valve electrical connection that this liquid level detecting sensor and external pipe are provided with realizes automatically controlling, the air intake that described evaporimeter 3 top is provided with is communicated with the steam outlet of steam box 1, the water inlet be provided with bottom described evaporimeter 3 is communicated with the delivery port of storage tank 6, the steam drain 13 that described evaporimeter 3 top is provided with is communicated with the air intake of the second separator 5, and the steam drain 13 of described second separator 5 is communicated with the air intake of steam box 1.Described water source regeneration unit comprises the first separator 2, the water inlet of described first separator 2 is connected with the discharge outlet be provided with bottom evaporimeter 3, the delivery port of described first separator 2 is connected with the regeneration water source water inlet of storage tank 6, and the top of described first separator 2 is provided with air discharge ports 12.
The first water pump 9 is provided with between evaporimeter 3 and storage tank 6, temperature sensor 8 is provided with between described first water pump 9 and storage tank 6, the temperature that storage tank 6 flows to the water of evaporimeter 3 is detected by temperature sensor 8, and detection numerical value is sent to control centre, control centre controls the rotating speed of the first water pump 9 according to temperature value, in order to ensure the water at low temperature vapour-liquid blending water that formation temperature is higher after evaporator 3 heat exchange, when temperature sensor 8 detect storage tank 6 flow to the temperature of the water of evaporimeter 3 lower time, the rotor of the first water pump 9 is at low speed, now the transporting velocity of water at low temperature is lower, extend the heat exchanger time of water at low temperature, and then improve heat exchange effect.
Between described first separator and storage tank 6, be provided with the second water pump 10, be provided with filter 4 between described second water pump 10 and storage tank 6, the Impurity removal in the aqueous water that recovered steam is formed by this filter 4 after evaporator 3 falls to be formed pure regeneration water source.
The air discharge ports 12 of described first separator is connected with vacuum blower 11, because vacuum blower can create vacuum environment, therefore vacuum blower 11 provides outputting power for high-temperature steam, ensure that the smooth and easy output of high-temperature steam, in addition, the air contained in high-temperature steam also can be got rid of by vacuum blower 11, ensure that the air content at regeneration water source maintains in certain limit.
Roots blower 7 is provided with between the second separator 5 and steam box 1, in life, in steam box 1 steam temperature requirement about 110 DEG C, pressure is between 120-140kpa, the temperature of water at low temperature after heat exchange is about 85 DEG C, therefore the roots blower 7 be provided with can heat the steam be separated through the second separator and pressurizes before flowing to steam box 1, and then meets temperature requirement and the pressure requirements of steam box 1 steam used.
A steam regeneration power-economizing method for applying steam regenerating energy-saving system, the steps include:
First the high-temperature steam that steam box 1 discharges is transported in evaporimeter 3, heat exchange is carried out with the water at low temperature inputted by storage tank 6 in evaporimeter 3, water at low temperature presents the vapour-liquid admixture of high temperature after heat exchange, high-temperature steam condenses into aqueous water simultaneously, after heat exchange, high-temperature water in vapour-liquid admixture carries the second separator 5, by the second separator 5, the vapour-liquid of high temperature mixing water source is carried out vapor-liquid separation, vapor portion in vapour-liquid mixing water source is transported to steam box 1 and utilizes, aqueous water part in vapour-liquid mixing water source is transported to evaporimeter 4 and carries out heat exchange again, complete the recycling of the steam heat discharged by steam box 1 thus, meanwhile, the aqueous water that high-temperature steam condenses after evaporator 3 heat exchange is delivered to storage tank 6 through the first separator 2 and recycles, in this recycled water and storage tank 6, the mixing of deposit water recycles, and finally flow to steam box 1 in vapour form, complete recovery and the utilization of moisture in the high-temperature steam discharged by steam box 1.
In order to ensure that the steam to steam box conveying is high temperature and high pressure steam, utilizing roots blower 7 heat before flowing to steam box the steam by vapor-liquid separation organizational separation and pressurize, and then meeting steam box to the temperature requirement of steam and pressure requirements
The foregoing is only preferred embodiment of the present invention, not in order to limit the present invention, within the spirit and principles in the present invention all, any amendment done, equivalent replacement, improvement etc., all should be included within protection scope of the present invention.
Claims (10)
1. a steam regeneration energy conserving system, it is characterized in that: this system is applied to steam box, described steam regeneration energy conserving system comprises steam regeneration unit, water source regeneration unit and connecting pipe, described steam regeneration unit comprises evaporimeter and vapor-liquid separation mechanism, the air intake that described evaporimeter top is provided with is communicated with the steam outlet of steam box, the water inlet that described base of evaporator is provided with is communicated with the delivery port of vapor-liquid separation mechanism, the steam drain that described evaporimeter top is provided with is communicated with the air intake of vapor-liquid separation mechanism, the steam drain that described vapor-liquid separation mechanism is provided with is communicated with the air intake of steam box, described vapor-liquid separation mechanism is provided with external pipe, vapor-liquid separation mechanism is connected by external pipe and external water source,
Described water source regeneration unit comprises the first separator, and the water inlet of described first separator is connected with the discharge outlet that base of evaporator is provided with, and the regeneration water source water inlet that delivery port and the vapor-liquid separation mechanism of described first separator are provided with is connected.
2. a kind of steam regeneration energy conserving system according to claim 1, it is characterized in that: described vapor-liquid separation mechanism comprises storage tank and the second separator, described second separator is arranged on directly over storage tank, and described second separator is connected with storage tank, ensure that the aqueous water be separated through the second separator flow in storage tank thus, the delivery port of described vapor-liquid separation mechanism, regeneration water source water inlet and external pipe are separately positioned on storage tank, and air intake and the steam drain of described vapor-liquid separation mechanism are arranged on the second separator.
3. a kind of steam regeneration energy conserving system according to claim 2, is characterized in that: be provided with liquid level gauge in described storage tank, by the height of water level in liquid level gauge observation storage tank.
4. a kind of steam regeneration energy conserving system according to claim 1 and 2, is characterized in that: at evaporimeter with vapor-liquid separation is inter-agency is provided with the first water pump, described first water pump and vapor-liquid separation is inter-agency is provided with temperature sensor.
5. a kind of steam regeneration energy conserving system according to claim 1 and 2, it is characterized in that: described first separator and vapor-liquid separation is inter-agency is provided with the second water pump, described second water pump and vapor-liquid separation is inter-agency is provided with filter, the Impurity removal in the aqueous water that recovered steam is formed by this filter after evaporator falls to be formed pure regeneration water source.
6. a kind of steam regeneration energy conserving system according to claim 1 and 2, is characterized in that: the top of described first separator is provided with air discharge ports, and described air discharge ports is connected with vacuum blower.
7. a kind of steam regeneration energy conserving system according to claim 1 and 2, is characterized in that: described evaporimeter is plate type heat exchanger.
8. a kind of steam regeneration energy conserving system according to claim 1 and 2, it is characterized in that: between vapor-liquid separation mechanism and steam box, be provided with roots blower, this roots blower can heat the steam through vapor-liquid separation organizational separation and pressurize before flowing to steam box, and then meets temperature requirement and the pressure requirements of steam box steam used.
9. application rights requires a steam regeneration power-economizing method for steam regeneration energy conserving system described in 1, it is characterized in that: comprise the following steps:
1), heat exchanging step: the high-temperature steam that steam box discharges is transported in evaporimeter, heat exchange is carried out with the water at low temperature inputted by vapor-liquid separation mechanism in evaporimeter, water at low temperature presents the vapour-liquid admixture of high temperature after heat exchange, and high-temperature steam condenses into aqueous water simultaneously;
2), the recycling step at the vapour-liquid mixing water source of high temperature: the vapour-liquid of high temperature mixing water source is carried out vapor-liquid separation by vapor-liquid separation mechanism, vapor portion in vapour-liquid mixing water source is transported to steam box and utilizes, aqueous water part in vapour-liquid mixing water source is transported to evaporimeter and carries out heat exchange again, completes the recycling of the steam heat discharged by steam box thus;
3) moisture, in high-temperature steam utilize step: high-temperature steam is condensed into aqueous water after evaporator heat exchange, this aqueous water is delivered to vapor-liquid separation mechanism through separator, be delivered to evaporimeter through vapor-liquid separation mechanism and carry out heat exchange, and finally flow to steam box in vapour form, complete recovery and utilization that the water from steam that discharged by steam box divides.
10. a kind of steam regeneration power-economizing method according to claim 9, it is characterized in that: utilize roots blower heat before flowing to steam box the steam by vapor-liquid separation organizational separation and pressurize, and then meet steam box to the temperature requirement of steam and pressure requirements.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201510262162.7A CN104819446B (en) | 2015-05-20 | 2015-05-20 | Energy-saving steam regeneration system and method |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201510262162.7A CN104819446B (en) | 2015-05-20 | 2015-05-20 | Energy-saving steam regeneration system and method |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN104819446A true CN104819446A (en) | 2015-08-05 |
| CN104819446B CN104819446B (en) | 2017-01-11 |
Family
ID=53729828
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201510262162.7A Expired - Fee Related CN104819446B (en) | 2015-05-20 | 2015-05-20 | Energy-saving steam regeneration system and method |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN104819446B (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105953198A (en) * | 2016-06-05 | 2016-09-21 | 侴乔力 | Siphon-circulation exhaust heat steam boiler |
| CN106175429A (en) * | 2016-09-29 | 2016-12-07 | 广州广冷华旭制冷空调实业有限公司 | Steaming box device and steam condensing method thereof |
| CN108587844A (en) * | 2018-05-18 | 2018-09-28 | 安徽金种子酒业股份有限公司 | A kind of white spirit brewing steaming with pressure and Steam Recovery circulator |
Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2009097790A (en) * | 2007-10-17 | 2009-05-07 | Kameyama Tekkosho:Kk | Steam generator |
| JP2010002057A (en) * | 2008-06-18 | 2010-01-07 | Miura Co Ltd | Clean steam generator |
| KR100947048B1 (en) * | 2009-10-05 | 2010-03-10 | (주)우신비엔피 | Recycling system of high temperature condensed water |
| JP2013057412A (en) * | 2011-09-07 | 2013-03-28 | Ishin Giken:Kk | Method of operating pure vapor generating apparatus |
| CN103196132A (en) * | 2013-04-03 | 2013-07-10 | 中国石油天然气股份有限公司 | Recovery technology for steam atomizing oil condensed water of viscous oil tank truck |
| CN103604233A (en) * | 2013-11-19 | 2014-02-26 | 陕西华泰厨房设备有限公司 | Process and system for using waste heat of steam of steam box |
| CN204678301U (en) * | 2015-05-20 | 2015-09-30 | 天津鑫玛新能源科技有限公司 | A kind of steam regeneration energy conserving system |
-
2015
- 2015-05-20 CN CN201510262162.7A patent/CN104819446B/en not_active Expired - Fee Related
Patent Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2009097790A (en) * | 2007-10-17 | 2009-05-07 | Kameyama Tekkosho:Kk | Steam generator |
| JP2010002057A (en) * | 2008-06-18 | 2010-01-07 | Miura Co Ltd | Clean steam generator |
| KR100947048B1 (en) * | 2009-10-05 | 2010-03-10 | (주)우신비엔피 | Recycling system of high temperature condensed water |
| JP2013057412A (en) * | 2011-09-07 | 2013-03-28 | Ishin Giken:Kk | Method of operating pure vapor generating apparatus |
| CN103196132A (en) * | 2013-04-03 | 2013-07-10 | 中国石油天然气股份有限公司 | Recovery technology for steam atomizing oil condensed water of viscous oil tank truck |
| CN103604233A (en) * | 2013-11-19 | 2014-02-26 | 陕西华泰厨房设备有限公司 | Process and system for using waste heat of steam of steam box |
| CN204678301U (en) * | 2015-05-20 | 2015-09-30 | 天津鑫玛新能源科技有限公司 | A kind of steam regeneration energy conserving system |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105953198A (en) * | 2016-06-05 | 2016-09-21 | 侴乔力 | Siphon-circulation exhaust heat steam boiler |
| CN106175429A (en) * | 2016-09-29 | 2016-12-07 | 广州广冷华旭制冷空调实业有限公司 | Steaming box device and steam condensing method thereof |
| CN106175429B (en) * | 2016-09-29 | 2018-06-29 | 广州广冷华旭制冷空调实业有限公司 | Steaming box device and its steam condensing method |
| CN108587844A (en) * | 2018-05-18 | 2018-09-28 | 安徽金种子酒业股份有限公司 | A kind of white spirit brewing steaming with pressure and Steam Recovery circulator |
Also Published As
| Publication number | Publication date |
|---|---|
| CN104819446B (en) | 2017-01-11 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN204034286U (en) | Board-like mechanical vapour recompression evaporator | |
| CN104819446A (en) | Energy-saving steam regeneration system and method | |
| CN103301640B (en) | Concentration method and device for traditional Chinese medicine extracting solution | |
| CN207279602U (en) | A kind of closed type condensate water recovery device | |
| CN101966396A (en) | Evaporation device | |
| CN207161279U (en) | A kind of energy-saving steam waste heat recovery device | |
| CN204891253U (en) | Evaporative concentration system of emulsion | |
| CN203095629U (en) | Sodium chloride recycling and crystallizing device | |
| CN201250219Y (en) | Internal circulating vacuum oil cleaning device | |
| CN204678301U (en) | A kind of steam regeneration energy conserving system | |
| CN208426672U (en) | A kind of steam condensate recovery system | |
| CN204352224U (en) | A kind of energy-saving high vacuum autoclave with pulsing system | |
| CN108654127A (en) | A kind of steam condensate recovery system | |
| CN201216884Y (en) | Energy-conservation forced-air circulation liquid extract concentrating device | |
| CN103055536A (en) | Heat reflux extraction and concentration equipment | |
| CN206995895U (en) | MVR traditional Chinese drug inspissation systems with defoaming function | |
| CN204841338U (en) | Gas liquid separation device | |
| CN208770862U (en) | Interior heat cycles vaporising device and vapo(u)rization system | |
| CN201906471U (en) | Vacuum concentration device for diluted acid | |
| CN101870502B (en) | Space water treatment vaporization system | |
| CN205205926U (en) | Device of system water in follow air | |
| CN105466163B (en) | A kind of vegetables low temperature molecular dehydration energy saving drying equipment | |
| CN206011335U (en) | Bamboo and wood products's Oleum Verniciae fordii heat-treatment production line oil temperature cyclic control system | |
| CN205151879U (en) | Biochemical pond intensification system of air compressor machine waste heat retrieves | |
| CN204745696U (en) | High boiling point rises material evaporative concentration system |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| EXSB | Decision made by sipo to initiate substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20170111 Termination date: 20190520 |