CN2745367Y - Technological equipment for extracting hawthorn fruit kernel raw juice - Google Patents
Technological equipment for extracting hawthorn fruit kernel raw juice Download PDFInfo
- Publication number
- CN2745367Y CN2745367Y CN 200320104262 CN200320104262U CN2745367Y CN 2745367 Y CN2745367 Y CN 2745367Y CN 200320104262 CN200320104262 CN 200320104262 CN 200320104262 U CN200320104262 U CN 200320104262U CN 2745367 Y CN2745367 Y CN 2745367Y
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- hawthorn fruit
- extracting
- distillation
- raw juice
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Abstract
The utility model discloses a technological device for extracting hawthorn fruit kernel raw juice, belonging to the processing apparatus for extracting raw juice. Heating pyrogens are fixed outside a distillation extracting kettle whose top part is provided with a material inlet, a bile duct and a thermometer, and a waste outlet is arranged at the bottom of the distillation extracting kettle. The upper part of the bile duct is connected with a delivery tube which is connected in series with a condensate pipe and a liquid material outlet thereof. A condenser which is sheathed outside the condensate pipe comprises a circulating water inlet, a circulating water outlet, a condensate circulating water pump and a connecting cycle pump. The technological device for extracting hawthorn fruit kernel raw juice of the utility model has strong corrosion resistance of the steel stove because the stove body of the distillation extracting kettle is made of thickening stainless steels; the utility model improves the conduit, adds a thermal insulation interlayer and the delivery tube, automatically controls circulating water, reduces producing procedure, enhances yield quality and simultaneously extracts raw juice under stable temperature safely.
Description
Technical field
The utility model belongs to the process equipment that extracts stoste, refers in particular to the new technical equipment that a kind of hawthorn fruit stone stoste is extracted.
Background technology
In existing association area application technology equipment, comprise with the process equipment major part described in the open source literature being that directly-heated type is extracted by the condensation of vapour cigarette importing bile duct, and multistage heats up and to squeeze under the continuous high temperature between 100 to 480 ℃, cut gets the liquid material, existing application apparatus structure is too simple, be easy to make, but there is not safe practice facility member, in process of production because of equipment high temperature cut, bile duct, condensing plant does not possess automatic cold water circulation safety control device, easily cause blast, the explosion phenomenon of hurting sb.'s feelings is very general, and makes great amount of water resources waste, heat supply energy waste, output capacity is low, can not finish large-scale regular industrialization safety in production.
Still unmatchful hawthorn fruit stone extracts equipment and technology renewal or more perfect report in the prior art, therefore need further improve the existing equipment technology, promptly is the technology that the present invention will solve.
Summary of the invention
The purpose of this utility model is to overcome the deficiencies in the prior art, the new technical equipment that provides a kind of hawthorn fruit stone stoste to extract.It is characterized in that: described hawthorn fruit stone stoste is extracted the fixed outside heating pyrogen of the distillation extraction still of equipment, and the top of extracting still in distillation is provided with feeding mouth, bile duct and thermometer, and the bottom is provided with waste outlet; The bile duct upper end connects delivery line, and delivery line is connected in series with condensate pipe and the outlet of liquid material thereof again, and condenser is enclosed within the condensate pipe outside, and the recirculated water import and export of condenser is connected with the condensed water circulating pump; The condensed water circulating pump is installed in the condensate draining, and tank moisturizing gateway and automatic control alarm device are installed in the bottom of condensate draining; Also be surrounded by asbestos insulation interlayer and delivery line outer tube in the delivery line outside.
The utility model beneficial effect is 1. to have increased the reasonable connection of automatically recycled water equipment and the improvement of conduit, has improved the safety guarantee of equipment in the operation running, and can realize the large industrialized safety in production; 2, the consumption and the heat supply energy resource consumption of water resource have been reduced; 3, improved output capacity and output quality, and can be according to multiplying arrangement 10-20 times in proportion of enterprise's production scale; 4, this equipment is of many uses, but the extraction of production and processing fruit stone class, seed, beans, plant, and but derived product comprises medicine, health care, sterilization, food, washing, health product, do not need to add any entrainer in leaching process, to guarantee the pure natural property of extract.
Description of drawings
Fig. 1 extracts the still structural representation for distillation.
Fig. 2 is another structural representation of Fig. 1.
The specific embodiment
The new technical equipment that the utility model provides a kind of hawthorn fruit stone stoste to extract.Under engage accompanying drawing the utility model illustrated.
Shown in Figure 1, distillation is extracted still and is made up of body of heater outer 1 and body of heater internal layer 3, fixing heating pyrogen 2 between body of heater outer 1 and body of heater internal layer 3, the top of extracting still is provided with feeding mouth 10, bile duct 4 stretches in the distillation extraction still from the top of distillation extraction still distilling, the thermometer 12 that is connected with thermometer 13 inserts in the distillation extraction still from the top that still is extracted in distillation, and distillation is extracted the still bottom and is provided with waste outlet 11; Bile duct 4 upper ends connect delivery line 5, delivery line 5 is connected in series with condensate pipe 8 and liquid material outlet 14 thereof again, condenser 9 is enclosed within condensate pipe 8 outsides, the circulating water intake 15 of condenser, circulating water outlet 16 are connected respectively to the lower end and the upper end of condenser 9, condensed water circulating pump 17 is installed in the condensate draining 18, and tank moisturizing gateway 19 and automatic control alarm device 20 are installed in the bottom of condensate draining 18.Also be surrounded by asbestos insulation interlayer 6 and delivery line outer tube 7 in delivery line 5 outsides.
Figure 2 shows that another structural representation of distillation extraction still.Its structure and Fig. 1 are basic identical, and what they were different is that recirculated water 24 directly enters condensate draining 18 from circulating water pipe 22; The temperature controller 2 21 of She Zhiing is contained in condenser and steam delivery line junction in addition.On liquid material outlet 14, preformed hole 23 is set also.
Above-mentioned distillation is extracted the body of heater of still and is made of the stainless steel of thick 22-26mm, because the liquid material contains acidity, thicker stainless steel body of heater can extend using period.Its delivery line has increased inside and outside two-layer, and is middle for insulation is incubated interlayer with asbestos, reduced the loss of the heat supply energy in the middle of production technology.Vapor-permeable hole size on the bile duct is reduced to 0.5-1.5mm, (the hawthorn fruit stone enters the stokehold to make the raising of liquid material degree of purity, carried out pulverization process) greatest improvement is to have increased recirculated water equipment to be connected with the reasonable of condenser pipe, condenser, thereby promoted the function of equipment integral body, avoided original technical equipment can not circulate automatically and combine with water, condensation pipe because of condenser, the phenomenon so often appearance blast, explosion are hurted sb.'s feelings has ensured the safety of workman in production operation.
The utility model is the new technical equipment that a kind of hawthorn fruit stone stoste is extracted, be to be that raw material is produced stoste with the hawthorn fruit stone, the process of producing of its stoste is: select high-quality hawthorn fruit stone, clear water is rinsed well, be ground into fine grained, then with powder and water by 1: 1-1: 5 weight ratio is mixed, after soaking 4-10 hour, with the raw material that soaks from feeding mouth is packed gas retort into, close the furnace charge mouth, get final product firing up, burning things which may cause a fire disaster is an electric heating, natural gas, coal gas all can, heat up gradually and can remain under this temperature 95 ℃-100 ℃ (having increased inside and outside two-layer and insulation interlayer) because of having improved delivery line, to collect the rough liquid of hawthorn fruit stone, the rough liquid of collecting is carried out the destructive distillation second time again, temperature is 105 ℃-110 ℃, remain under this temperature, extract refined liquid through destructive distillation, again refined liquid distilled extraction, temperature at 105 ℃-110 ℃ to collect, hawthorn fruit stone stoste is product of the present invention.
The utility model can amplify the distillation still body of heater according to production scale, circulating pump and corollary equipment.Extracting the cut volume is that the 60-120 ml/min is to the 600-1200 ml/min.Volume is 10000 to 200000 milliliters.
Claims (2)
1. the new technical equipment that extracts of a hawthorn fruit stone stoste, it is characterized in that: described hawthorn fruit stone stoste is extracted the fixed outside heating pyrogen of the distillation extraction still of equipment, the top of extracting still in distillation is provided with feeding mouth, bile duct and thermometer, and the bottom is provided with waste outlet; The bile duct upper end connects delivery line, and delivery line is connected in series with condensate pipe and the outlet of liquid material thereof again, and condenser is enclosed within the condensate pipe outside, and the recirculated water import and export of condenser is connected with the condensed water circulating pump; The condensed water circulating pump is installed in the condensate draining, and tank moisturizing gateway and automatic control alarm device are installed in the bottom of condensate draining; Also be surrounded by asbestos insulation interlayer and delivery line outer tube in the delivery line outside.
2. the new technical equipment that a kind of hawthorn fruit stone stoste according to claim 1 is extracted is characterized in that: the extraction cut volume that still is extracted in described distillation be the 60-120 ml/min to the 600-1200 ml/min, volume is 10000 to 200000 milliliters.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 200320104262 CN2745367Y (en) | 2003-12-31 | 2003-12-31 | Technological equipment for extracting hawthorn fruit kernel raw juice |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 200320104262 CN2745367Y (en) | 2003-12-31 | 2003-12-31 | Technological equipment for extracting hawthorn fruit kernel raw juice |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN2745367Y true CN2745367Y (en) | 2005-12-14 |
Family
ID=35581958
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 200320104262 Expired - Fee Related CN2745367Y (en) | 2003-12-31 | 2003-12-31 | Technological equipment for extracting hawthorn fruit kernel raw juice |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN2745367Y (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102350072A (en) * | 2011-09-02 | 2012-02-15 | 江苏斯威森生物医药工程研究中心有限公司 | Vacuum reduced pressure concentration system |
| CN102350063A (en) * | 2011-09-02 | 2012-02-15 | 江苏斯威森生物医药工程研究中心有限公司 | Vacuum decompressing concentrating system |
| CN110923056A (en) * | 2019-12-13 | 2020-03-27 | 北京多宝德健康科技产业发展有限公司 | Method and device for dry distillation of hawthorn seed extracting solution |
-
2003
- 2003-12-31 CN CN 200320104262 patent/CN2745367Y/en not_active Expired - Fee Related
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102350072A (en) * | 2011-09-02 | 2012-02-15 | 江苏斯威森生物医药工程研究中心有限公司 | Vacuum reduced pressure concentration system |
| CN102350063A (en) * | 2011-09-02 | 2012-02-15 | 江苏斯威森生物医药工程研究中心有限公司 | Vacuum decompressing concentrating system |
| CN110923056A (en) * | 2019-12-13 | 2020-03-27 | 北京多宝德健康科技产业发展有限公司 | Method and device for dry distillation of hawthorn seed extracting solution |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C19 | Lapse of patent right due to non-payment of the annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |