CN87101339A - Vacuum far infrared concentrator - Google Patents
Vacuum far infrared concentrator Download PDFInfo
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- CN87101339A CN87101339A CN 87101339 CN87101339A CN87101339A CN 87101339 A CN87101339 A CN 87101339A CN 87101339 CN87101339 CN 87101339 CN 87101339 A CN87101339 A CN 87101339A CN 87101339 A CN87101339 A CN 87101339A
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- heating
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Abstract
Vacuum far infrared concentrator is a kind of novel vacuum evaporation, vacuum concentration equipment.Have simple in structure, use convenient, volume is little, corrosion resistance and good, low power consumption and other advantages.
This equipment is owing to adopt the form of heating in the far infrared, can reduce at present with boiler and steam condensing plant in the outer heating form of steam, its heating system is simplified, not only be convenient to operation, and provide condition for popularization and application vacuum evaporation and vacuum novel concentrating process.
Description
The present invention is a kind of novel vacuum evaporation and vacuum concentration equipment.The vacuum evaporation, the vacuum that are mainly used in various liquid in the industry such as chemical industry, pharmacy, sugaring concentrate among the production technology; Concentrate with the low temperature of various fruit juice, vegetable juice, milk; And Chinese medicine decoct lixiviate and evaporation and concentration.
Vacuum evaporation at present for a change, concentrated production equipment adopt in the Steam Heating method, the equipment that exists is huge, cost is high, energy consumption is high and be difficult for shortcoming such as popularization and application, with the deep processing ability of and Chinese medicinal herbs concentrated, the food industry and the herbal pharmaceutical industrial expansion of promotion China, and invented this vacuum far infrared concentrator for the low-temperature evaporation that enlarges various fruit syrup, vegetable juice.
The present invention mainly contains vacuum chamber, Far-infrared Heating and temperature control system, and vacuum acquiring system is formed.Different according to the different and enrichment that will reach of the liquid material that is evaporated, concentrates are designed to the form of Far-infrared Heating again direct-fired version.As shown in Figure 1 and the version of water-bath heating as shown in Figure 2.Direct-heating type is mainly used in and requires to reach the low liquid of enrichment.The water-bath heated type is mainly used in and requires to reach decocting and concentrating of high liquid of enrichment and Chinese medicinal herbs.
Vacuum chamber is a main body of the present invention, because the manufacturing of its useful ceramics material, thereby improved decay resistance, reduce the loss energy savings of heat.
The Far-infrared Heating temperature control system is the mechanism of required vaporization heat in feed fluid evaporation of the present invention, the concentration process, is made up of enamel far-infrared element, thermometric thermal sensible element, temperature control instrument and electric elements.Owing to adopt the mode of heating in the far-infrared element.Thereby improved utilization efficiency of heat energy.Because the effect of temperature control system can make the liquid in the vacuum chamber remain within the temperature required scope, reduces heat-energy losses.The temperature control system of direct-heating type is that the temperature control system of directly controlling the water-bath heated type of fluid temperature is to control fluid temperature indirectly by the indoor water temperature of control water-bath.
Vacuum acquiring system is the mechanism that the present invention makes vacuum chamber obtain and keep required vacuum, is made up of water pump, water flow jet vavuum pump, cyclic water tank, vacuum line etc.Because the water flow jet vavuum pump has the performance of condensed steam, can reduce the steam condensing plant in the vacuum acquiring system.
The present invention realizes that vacuum evaporation, concentrated purpose are to lean against to be evaporated concentrated liquid in the vacuum chamber, when supplying with required vaporization heat by far infrared heating system, in time the water vapour that is produced in the vacuum chamber is extracted by vacuum acquiring system again, make the vacuum chamber acquisition and keep required vacuum to reach.
That the present invention has is simple in structure, easy to operate, volume is little, corrosion resistance and good, applied range, low power consumption and other advantages.
Principal character of the present invention is: owing to adopt the form of enamel far infrared heating and interior heating, can improve the conversion and the absorption efficiency of heat energy, energy savings.In order to replace the mode of the outer heating of present steam, can reduce boiler and steam condensing plant, its heating system is simplified.Because temperature control system can make the temperature of vacuum chamber be controlled within the required scope, can guarantee product quality, again by reducing thermal loss.
Further feature of the present invention is: because the form of heating in adopting, vacuum chamber can adopt the ceramic material of decay resistance and good heat insulating, has not only simplified the structure of vacuum chamber, reduces cost, and can improve decay resistance and reduce heat-energy losses.
Of the present invention is owing to adopt the water flow jet vavuum pump by a feature, and vacuum acquiring system is simplified, and reduces steam condensing plant.
The present invention will have wide application future owing to possess above-mentioned advantage.
Claims (6)
1, a kind of vacuum far infrared concentrator, principal character of the present invention is: formed direct-heating type and two kinds of different structure forms of water-bath heated type by vacuum chamber, Far-infrared Heating and temperature control system, vacuum acquiring system.
2, require said vacuum chamber in 1 according to claim, it is characterized in that: the useful ceramics material is made, to improve decay resistance and to reduce heat-energy losses.
3, require said vacuum acquiring system in 1 according to claim, it is characterized in that: formed by water pump, water flow jet vavuum pump, cyclic water tank, vacuum line, because the water flow jet vavuum pump has the performance of condensed steam, can reduce the steam condensing plant in vacuum acquiring system.
4, require said Far-infrared Heating and temperature control system among me according to claim, it is characterized in that: form by enamel far-infrared element thermometric thermal sensible element, temperature control instrument and electric elements.The enamel far-infrared element is installed in the vacuum chamber,, can improves utilization efficiency of heat energy owing to adopt the mode of this interior heating.Temperature control system can be controlled at the fluid temperature in the vacuum chamber temperature required, energy savings.
5, require the version of said direct-heating type in 1 according to claim, it is characterized in that: far-infrared element is installed in the vacuum chamber, and directly to being evaporated concentrated liquid heating, the heating process of this heat form is comparatively fierce, and speed of production is very fast.
6, require the version of said water-bath heated type in 1 according to claim.It is characterized in that: far infrared heating is installed in the water-bath heating clamber, is that the water in the water-bath heating clamber is heated, and heats being evaporated concentrated liquid in the vacuum chamber by water and water-bath chamber body again.The heating process of this heat form is comparatively gentle, mainly solves because of strength of fluid when high the coking phenomenon that is produced in heating process.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN 87101339 CN87101339A (en) | 1987-05-21 | 1987-05-21 | Vacuum far infrared concentrator |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN 87101339 CN87101339A (en) | 1987-05-21 | 1987-05-21 | Vacuum far infrared concentrator |
Publications (1)
Publication Number | Publication Date |
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CN87101339A true CN87101339A (en) | 1988-12-07 |
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Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
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CN 87101339 Pending CN87101339A (en) | 1987-05-21 | 1987-05-21 | Vacuum far infrared concentrator |
Country Status (1)
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CN (1) | CN87101339A (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN103007557A (en) * | 2012-12-25 | 2013-04-03 | 韦丽梅 | Low-temperature vacuum concentration device for plant extracts |
CN103028266A (en) * | 2012-12-25 | 2013-04-10 | 韦丽梅 | Control method of low-temperature vacuum concentration device for plant extract |
CN104208885A (en) * | 2014-09-23 | 2014-12-17 | 山东滨州智晟科技创新促进中心 | D-ribose concentration apparatus and process |
-
1987
- 1987-05-21 CN CN 87101339 patent/CN87101339A/en active Pending
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN103007557A (en) * | 2012-12-25 | 2013-04-03 | 韦丽梅 | Low-temperature vacuum concentration device for plant extracts |
CN103028266A (en) * | 2012-12-25 | 2013-04-10 | 韦丽梅 | Control method of low-temperature vacuum concentration device for plant extract |
CN104208885A (en) * | 2014-09-23 | 2014-12-17 | 山东滨州智晟科技创新促进中心 | D-ribose concentration apparatus and process |
CN104208885B (en) * | 2014-09-23 | 2016-02-03 | 山东滨州智晟科技创新促进中心 | A kind of D-ribose enrichment facility and technique |
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WD01 | Invention patent application deemed withdrawn after publication |