CN105363232A - High-viscosity high-concentration tomato sauce production device - Google Patents
High-viscosity high-concentration tomato sauce production device Download PDFInfo
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- CN105363232A CN105363232A CN201510902464.6A CN201510902464A CN105363232A CN 105363232 A CN105363232 A CN 105363232A CN 201510902464 A CN201510902464 A CN 201510902464A CN 105363232 A CN105363232 A CN 105363232A
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Abstract
The invention discloses a high-viscosity high-concentration tomato sauce production device. The high-viscosity high-concentration tomato sauce production device comprises a preheating tank, a single effect first segment evaporator, a single effect second segment evaporator, a double-effect evaporator, and a triple effect evaporator; the top of the preheating tank is connected with a feeding pipe, and the bottom is connected with the triple effect evaporator, the double-effect evaporator, the single effect second segment evaporator, and the single effect first segment evaporator successively via a conveying pipe; a first feeding pump, a second feeding pump, a third feeding pump, and a fourth feeding pump are arranged between the single effect first segment evaporator and the single effect second segment evaporator, the single effect second segment evaporator and the double-effect evaporator, the double-effect evaporator and the triple effect evaporator, and the triple effect evaporator and the preheating tank respectively; the bottom of the single effect second segment evaporator is connected with a discharging pump; and the upper parts of the single effect first segment evaporator, the single effect second segment evaporator, the double-effect evaporator, and the triple effect evaporator are connected with a steam pipeline respectively. Tomato sauce produced using the high-viscosity high-concentration tomato sauce production device is high in viscosity and concentration, and product quality is improved.
Description
Technical field
The present invention relates to tomato paste production equipment, particularly relate to a kind of high viscosity heavy tomato puree process units.
Background technology
At present, the export processing industry fast development of tomato in China and goods thereof, China has become the very important tomato product producing country in the whole world and exported country.Therefore, the Quality and yield improving catsup is need the problem of solution at present badly to adapt to the growing market demand.And the Quality and yield of equipment on catsup producing catsup has very large impact.
Existing catsup production technology comprises the following steps: after catsup enters production line, first carries out cleaning, selecting, then broken, then sends to making beating, and obtained concentration is the tomato juice of 4 ~ 5wt%.Tomato juice is sent in evaporimeter and is concentrated, obtained catsup, and then through sterilization, cooling, carries out sterile filling, obtains finished product catsup.But in the actual production process of catsup, be difficult to the heavy tomato puree that obtained viscosity is higher, the demand in market can not be met.
Summary of the invention
The object of this invention is to provide a kind of process units can preparing high viscosity, heavy tomato puree.
The object of the invention is to be achieved through the following technical solutions:
A kind of catsup enrichment facility, comprise preheating can and an effect one section of evaporimeter, one effect flash evaporator, 2nd effect evaporator and triple effect evaporator, described preheating can top is connected with feed pipe, bottom connects described triple effect evaporator successively by feed pipe, 2nd effect evaporator, the bottom of one effect flash evaporator and an effect one section of evaporimeter, and imitate between flash evaporator at described effect one section of evaporimeter and, between one effect flash evaporator and 2nd effect evaporator, feed pipe between 2nd effect evaporator and triple effect evaporator and between triple effect evaporator and preheating can is respectively arranged with 1-4 feeding engine, the bottom of a described effect flash evaporator also connects a discharging pump, the top of a described effect one section of evaporimeter, effect flash evaporator, 2nd effect evaporator and a triple effect evaporator connects jet chimney respectively, is separately installed with inlet valve at the steam inlet place of each evaporimeter, be provided with tube still heater in described preheating can, the steam inlet place of described tube still heater is provided with steam valve, and described preheating can is provided with pressure charging valve.
Preferably, to imitate between flash evaporator at described effect one section of evaporimeter 11 and one, one imitate and be also connected respectively by discharge pipe between flash evaporator with 2nd effect evaporator, between 2nd effect evaporator with triple effect evaporator, every section described, discharge pipe is respectively arranged with dump valve.
Beneficial effect of the present invention is as follows:
Owing to being provided with pressure charging valve on preheating can, can pressurize to preheating can, make temperature of charge reach rapidly the high temperature of 90 DEG C ~ 100 DEG C at short notice, make pectase passivation, thus make its viscosity reach 2.0-3.0cm/30s; In addition, each single-effect evaporator vacuum improves 30-40mmHg than in the past, temperature also correspondingly increases, make the concentration of catsup product reach 35-40wt%, improve the quality of product.
Accompanying drawing explanation
Fig. 1 is the structural representation of an embodiment of catsup enrichment facility of the present invention.
Detailed description of the invention
As shown in Figure 1, catsup enrichment facility of the present invention comprises preheating can 10 and an effect one section of evaporimeter 11, one effect flash evaporator 12, 2nd effect evaporator 13 and triple effect evaporator 14, preheating can 10 top is connected with feed pipe 15, bottom connects described triple effect evaporator 14 successively by feed pipe 16, 2nd effect evaporator 13, the bottom of one effect flash evaporator 12 and an effect one section of evaporimeter 11, and imitate between flash evaporator 12 at an effect one section of evaporimeter 11 and, between one effect flash evaporator 12 and 2nd effect evaporator 13, feed pipe 16 between 2nd effect evaporator 13 and triple effect evaporator 14 and between triple effect evaporator 14 and preheating can 10 is respectively arranged with 1-4 feeding engine 16a-16d.The bottom of one effect flash evaporator 12 also connects a discharging pump 20; The top that one effect, one section of evaporimeter 11, imitates flash evaporator 12,2nd effect evaporator 13 and triple effect evaporator 14 connects jet chimney 17 respectively, is separately installed with inlet valve 21 at the steam inlet place of each evaporimeter.Be provided with tube still heater in preheating can 10, the steam inlet place of described tube still heater is provided with steam valve, and described preheating can is provided with pressure charging valve.
In addition, to imitate between flash evaporator 12 at described effect one section of evaporimeter 11 and one, one imitate between flash evaporator 12 with 2nd effect evaporator 13, between 2nd effect evaporator 13 with triple effect evaporator 14 and can also be connected respectively by discharge pipe 18, every section described, discharge pipe 18 is respectively arranged with dump valve 19.
Utilize the process of this device production heavy tomato puree as follows:
By Hydraulic transportation, raw tomatoes material is delivered to scraper lifting machine to wash, raw material after washing is sent in flotation washer and is carried out secondary cleaning and choosing fruit, the raw material not meeting production requirement is selected, is then promoted by crushing screw precrushing, raw material is put into breakage pump and carries out fragmentation.Raw material through breakage pump fragmentation carries out the pre-heat treatment.Raw material after the pre-heat treatment carries out next operation again, in beater, namely carries out making beating filter, and by accomplishing fluently the catsup of slurry stored in making beating storage tank, then being sent in preheating can by slurry and carrying out instantaneous heating, improving its viscosity.
Afterwards slurry is concentrated.Saturated vapor can enter an effect one section of evaporimeter 11, effect flash evaporator 12,2nd effect evaporator 13 and triple effect evaporator 14 respectively by jet chimney 17.
In addition, imitate in flash evaporator 12 at an effect one section of evaporimeter 11, the juice vapour produced through heated material can enter in an effect flash evaporator 12 and 2nd effect evaporator 13 through discharge pipe 18 respectively, be used for post bake material, the juice vapour that 2nd effect evaporator 13 produces can enter triple effect evaporator 14 material through discharge line 18, is used for post bake material.
Concentrating through triple effect four sections of evaporimeters, the discharge concentration of catsup can reach 35-40wt%.
Claims (2)
1. a high viscosity heavy tomato puree process units, it is characterized in that: comprise preheating can (10) and an effect one section of evaporimeter (11), effect flash evaporator (12), 2nd effect evaporator (13) and triple effect evaporator (14)
Described preheating can (10) top is connected with feed pipe (15), bottom connects described triple effect evaporator (14) successively by feed pipe (16), 2nd effect evaporator (13), the bottom of one effect flash evaporator (12) and an effect one section of evaporimeter (11), and imitate between flash evaporator (12) described effect one section of evaporimeter (11) and, between one effect flash evaporator (12) and 2nd effect evaporator (13), feed pipe (16) between 2nd effect evaporator (13) and triple effect evaporator (14) and between triple effect evaporator (14) and preheating can (10) is respectively arranged with 1-4 feeding engine (16a-16d), the bottom of described effect flash evaporator (12) also connects a discharging pump (20),
A described effect one section of evaporimeter (11), a top of imitating flash evaporator (12), 2nd effect evaporator (13) and triple effect evaporator (14) connect jet chimney (17) respectively, are separately installed with inlet valve (21) at the steam inlet place of each evaporimeter;
Described preheating can is provided with tube still heater in (10), and the steam inlet place of described tube still heater is provided with steam valve, and described preheating can is provided with pressure charging valve.
2. catsup enrichment facility according to claim 1, it is characterized in that: described effect one section of evaporimeter (11) and imitates between flash evaporator (12), one imitate between flash evaporator (12) with 2nd effect evaporator (13), between 2nd effect evaporator (13) with triple effect evaporator (14) and be also connected respectively by discharge pipe (18), every section described, discharge pipe (18) is respectively arranged with dump valve (19).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201510902464.6A CN105363232A (en) | 2015-12-09 | 2015-12-09 | High-viscosity high-concentration tomato sauce production device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201510902464.6A CN105363232A (en) | 2015-12-09 | 2015-12-09 | High-viscosity high-concentration tomato sauce production device |
Publications (1)
| Publication Number | Publication Date |
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| CN105363232A true CN105363232A (en) | 2016-03-02 |
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| Application Number | Title | Priority Date | Filing Date |
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| CN201510902464.6A Pending CN105363232A (en) | 2015-12-09 | 2015-12-09 | High-viscosity high-concentration tomato sauce production device |
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Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4145265A (en) * | 1977-03-15 | 1979-03-20 | Asahi Glass Company, Ltd. | Process for concentration of caustic alkali solution produced by ion exchange membrane type electrolysis |
| CN201577499U (en) * | 2009-12-14 | 2010-09-15 | 甘肃省敦煌种业西域番茄制品有限公司 | Flash tank for ketchup production lines |
| CN101971962A (en) * | 2010-03-03 | 2011-02-16 | 中粮屯河股份有限公司 | Production method of super sticky hot-mashing tomato paste |
| CN101971963A (en) * | 2010-07-15 | 2011-02-16 | 上海神农机械有限公司 | Double-specification tomato paste production equipment |
| CN201752226U (en) * | 2010-07-15 | 2011-03-02 | 上海神农机械有限公司 | Production equipment for high-concentration catsup |
| CN205287653U (en) * | 2015-12-09 | 2016-06-08 | 天津威晟番茄制品有限公司 | High viscosity high concentration tomato ketchup apparatus for producing |
-
2015
- 2015-12-09 CN CN201510902464.6A patent/CN105363232A/en active Pending
Patent Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4145265A (en) * | 1977-03-15 | 1979-03-20 | Asahi Glass Company, Ltd. | Process for concentration of caustic alkali solution produced by ion exchange membrane type electrolysis |
| CN201577499U (en) * | 2009-12-14 | 2010-09-15 | 甘肃省敦煌种业西域番茄制品有限公司 | Flash tank for ketchup production lines |
| CN101971962A (en) * | 2010-03-03 | 2011-02-16 | 中粮屯河股份有限公司 | Production method of super sticky hot-mashing tomato paste |
| CN101971963A (en) * | 2010-07-15 | 2011-02-16 | 上海神农机械有限公司 | Double-specification tomato paste production equipment |
| CN201752226U (en) * | 2010-07-15 | 2011-03-02 | 上海神农机械有限公司 | Production equipment for high-concentration catsup |
| CN205287653U (en) * | 2015-12-09 | 2016-06-08 | 天津威晟番茄制品有限公司 | High viscosity high concentration tomato ketchup apparatus for producing |
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| C06 | Publication | ||
| PB01 | Publication | ||
| CB03 | Change of inventor or designer information |
Inventor after: Li Lian Inventor after: Chen Hongmao Inventor before: Wen Huaiyu Inventor before: Yi Li Inventor before: Wei Shuqiang Inventor before: Zhang Jinghui |
|
| COR | Change of bibliographic data | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| WD01 | Invention patent application deemed withdrawn after publication | ||
| WD01 | Invention patent application deemed withdrawn after publication |
Application publication date: 20160302 |