CN101779775B - Tomato skin, seed and residue dehydration drying and dry method skin and seed separation and combination production method in tomato paste factory - Google Patents
Tomato skin, seed and residue dehydration drying and dry method skin and seed separation and combination production method in tomato paste factory Download PDFInfo
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- CN101779775B CN101779775B CN2010101137855A CN201010113785A CN101779775B CN 101779775 B CN101779775 B CN 101779775B CN 2010101137855 A CN2010101137855 A CN 2010101137855A CN 201010113785 A CN201010113785 A CN 201010113785A CN 101779775 B CN101779775 B CN 101779775B
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- 235000007688 Lycopersicon esculentum Nutrition 0.000 title claims abstract description 60
- 240000003768 Solanum lycopersicum Species 0.000 title claims abstract description 60
- 238000001035 drying Methods 0.000 title claims abstract description 21
- 238000000034 method Methods 0.000 title claims abstract description 18
- 238000004519 manufacturing process Methods 0.000 title claims abstract description 12
- 238000000926 separation method Methods 0.000 title abstract description 4
- 230000018044 dehydration Effects 0.000 title abstract description 3
- 238000006297 dehydration reaction Methods 0.000 title abstract description 3
- 235000015113 tomato pastes and purées Nutrition 0.000 title abstract 3
- 239000000463 material Substances 0.000 claims abstract description 12
- 235000015112 vegetable and seed oil Nutrition 0.000 claims abstract description 8
- 239000010779 crude oil Substances 0.000 claims abstract description 7
- 238000005516 engineering process Methods 0.000 claims abstract description 7
- 238000007670 refining Methods 0.000 claims abstract description 6
- 239000002994 raw material Substances 0.000 claims abstract description 5
- 238000004332 deodorization Methods 0.000 claims abstract description 4
- 239000003921 oil Substances 0.000 claims abstract description 4
- 235000019198 oils Nutrition 0.000 claims abstract description 4
- 239000002245 particle Substances 0.000 claims abstract description 3
- 239000008158 vegetable oil Substances 0.000 claims abstract 2
- 239000002893 slag Substances 0.000 claims description 24
- 238000005469 granulation Methods 0.000 claims description 4
- 230000003179 granulation Effects 0.000 claims description 4
- 238000010009 beating Methods 0.000 claims description 3
- 238000007906 compression Methods 0.000 claims description 3
- 230000006835 compression Effects 0.000 claims description 3
- 238000007599 discharging Methods 0.000 claims description 3
- 239000000284 extract Substances 0.000 claims description 3
- 238000001914 filtration Methods 0.000 claims description 3
- 238000012856 packing Methods 0.000 claims description 3
- 238000004062 sedimentation Methods 0.000 claims description 3
- 206010013786 Dry skin Diseases 0.000 claims description 2
- 230000037336 dry skin Effects 0.000 claims description 2
- 235000012054 meals Nutrition 0.000 claims 1
- 238000003801 milling Methods 0.000 claims 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 abstract description 3
- 239000002351 wastewater Substances 0.000 abstract description 2
- 241000196324 Embryophyta Species 0.000 abstract 1
- 239000006185 dispersion Substances 0.000 abstract 1
- 230000007613 environmental effect Effects 0.000 abstract 1
- 235000012041 food component Nutrition 0.000 abstract 1
- 238000009776 industrial production Methods 0.000 abstract 1
- 238000004537 pulping Methods 0.000 abstract 1
- 230000001954 sterilising effect Effects 0.000 abstract 1
- 238000004659 sterilization and disinfection Methods 0.000 abstract 1
- UPYKUZBSLRQECL-UKMVMLAPSA-N Lycopene Natural products CC(=C/C=C/C=C(C)/C=C/C=C(C)/C=C/C1C(=C)CCCC1(C)C)C=CC=C(/C)C=CC2C(=C)CCCC2(C)C UPYKUZBSLRQECL-UKMVMLAPSA-N 0.000 description 3
- JEVVKJMRZMXFBT-XWDZUXABSA-N Lycophyll Natural products OC/C(=C/CC/C(=C\C=C\C(=C/C=C/C(=C\C=C\C=C(/C=C/C=C(\C=C\C=C(/CC/C=C(/CO)\C)\C)/C)\C)/C)\C)/C)/C JEVVKJMRZMXFBT-XWDZUXABSA-N 0.000 description 3
- 235000012661 lycopene Nutrition 0.000 description 3
- OAIJSZIZWZSQBC-GYZMGTAESA-N lycopene Chemical compound CC(C)=CCC\C(C)=C\C=C\C(\C)=C\C=C\C(\C)=C\C=C\C=C(/C)\C=C\C=C(/C)\C=C\C=C(/C)CCC=C(C)C OAIJSZIZWZSQBC-GYZMGTAESA-N 0.000 description 3
- 239000001751 lycopene Substances 0.000 description 3
- 229960004999 lycopene Drugs 0.000 description 3
- ZCIHMQAPACOQHT-ZGMPDRQDSA-N trans-isorenieratene Natural products CC(=C/C=C/C=C(C)/C=C/C=C(C)/C=C/c1c(C)ccc(C)c1C)C=CC=C(/C)C=Cc2c(C)ccc(C)c2C ZCIHMQAPACOQHT-ZGMPDRQDSA-N 0.000 description 3
- OENHQHLEOONYIE-UKMVMLAPSA-N all-trans beta-carotene Natural products CC=1CCCC(C)(C)C=1/C=C/C(/C)=C/C=C/C(/C)=C/C=C/C=C(C)C=CC=C(C)C=CC1=C(C)CCCC1(C)C OENHQHLEOONYIE-UKMVMLAPSA-N 0.000 description 2
- 239000005030 aluminium foil Substances 0.000 description 2
- 235000013734 beta-carotene Nutrition 0.000 description 2
- 239000011648 beta-carotene Substances 0.000 description 2
- TUPZEYHYWIEDIH-WAIFQNFQSA-N beta-carotene Natural products CC(=C/C=C/C=C(C)/C=C/C=C(C)/C=C/C1=C(C)CCCC1(C)C)C=CC=C(/C)C=CC2=CCCCC2(C)C TUPZEYHYWIEDIH-WAIFQNFQSA-N 0.000 description 2
- 229960002747 betacarotene Drugs 0.000 description 2
- 230000005484 gravity Effects 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- OENHQHLEOONYIE-JLTXGRSLSA-N β-Carotene Chemical compound CC=1CCCC(C)(C)C=1\C=C\C(\C)=C\C=C\C(\C)=C\C=C\C=C(/C)\C=C\C=C(/C)\C=C\C1=C(C)CCCC1(C)C OENHQHLEOONYIE-JLTXGRSLSA-N 0.000 description 2
- 230000015572 biosynthetic process Effects 0.000 description 1
- 239000000567 combustion gas Substances 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 238000003912 environmental pollution Methods 0.000 description 1
- 239000003337 fertilizer Substances 0.000 description 1
- 239000008187 granular material Substances 0.000 description 1
- 239000004519 grease Substances 0.000 description 1
- 238000005286 illumination Methods 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 238000000194 supercritical-fluid extraction Methods 0.000 description 1
- 238000003786 synthesis reaction Methods 0.000 description 1
Landscapes
- Fertilizers (AREA)
- Apparatuses For Bulk Treatment Of Fruits And Vegetables And Apparatuses For Preparing Feeds (AREA)
Abstract
The invention discloses a tomato skin, seed and residue dehydration drying and dry method skin and seed separation and combination production method in a tomato paste factory; the tomato skin, seed and residue obtained by pulping, peeling off and seed removal procedures in the tomato paste factory are used as raw materials, after wet skin, seed and residue are pre-dehydrated by adopting a squeezing method, a cocurrent rotary drum drier is adopted to dry the wet tomato skin, seed and residue with mixed skin and seed; and then a skin-seed rubbing dispersion device which is embedded between a material outlet of the drier and terminal dedusting equipment in series is adopted to separate the skin and seed; the separated skin is compressed to improve the density or high-pressure high-temperature disinfestation and sterilization is carried out to prepare into particles, and tomato seed crude oil and oil cakes are extracted from the separated seeds by adopting the equipment and technology in the existing vegetable oil plants, and the tomato seed crude oil is extracted only by degumming and deacidifying refining, in the way, the tomato skin, seed and residue can be processed in a large scale, so as to lead the comprehensive utilization of the tomato skin, seed and residue to realize industrial production; in addition, water does not need in the technology process, thereby greatly reducing the environmental protection of the tomato residue and completely eliminating the environment pollution of discharged waste water with high BOD and suspended matters in the technology of separating skin and seed with a wet process in the prior art; only degumming and deacidifying refining are carried out to the tomato seed crude oil, the decoloration and deodorization procedures in the deep refining are cancelled, so as to prevent oil rancidity, improve transparency and fully keep the commodity characteristics and nutritional components of the tomato seed oil.
Description
Technical field:
The invention belongs to the garden stuff processing technical field, the dehydrating and dry method skin seed discrete group combination production method of particularly a kind of catsup factory's tomato skin seed slag.
Background technology:
The catsup factory production capacity of China has reached more than 1,000,000 tons, and annual processing fresh tomato is more than 7,000,000 tons.Catsup factory every year less than 60 days production in, discharge about 400,000 tons of tomato skin seed slags.Tomato skin seed slag is moisture many, mixes bonding, is difficult to processing, lacks productivity set technique technology at present, is in the hygrometric state mixture is made feed, fertilizer or discarding state.
In the prior art,, the skin seed in the slag is separated a difficult problem, in water, separate the skin seed behind the general first thin up tomato skin seed slag, dehydrate the also employing CO that has after the wet separation dry band drier or the pneumatic drier of adopting of tomato skin seed slag
2Supercritical extraction unit extracts, purifying.But it is too high that the shortcoming of prior art is energy consumption, all do not consider drying and skin seed separable programming are made up and synthesis energy saving, is difficult to realize economy, the scale suitability for industrialized production of tomato skin seed slag.Cause over nearly 15 years, a large amount of valuable compositions are arranged, produce yet and utilize although people know in the tomato skin seed slag that catsup factory discharges.
Summary of the invention:
The objective of the invention is, dehydrating and dry method skin seed discrete group combination production method of a kind of catsup factory tomato skin seed slag is provided, can solve the industrial problems that tomato skin seed slag for comprehensive utilizes.
Technical scheme of the present invention is that dehydrate and the dry method skin seed discrete group combination production method of tomato skin seed slag comprise:
The tomato skin seed slag that goes the seed operation to discharge with the making beating of catsup factory is a raw material, and wet tomato skin seed slag adopts spiral press dewatering, makes its moisture content from more than 75%, drops to below 65%.Adopt the wet tomato skin seed slag of the dry skin seed of downflow type whizzer mixing shape then, whizzer has three layers of rotating cylinder, the rotating cylinder inwall all has the bowl-type flight of spiral layout, when drying machine rotates, material is taken up in the bottom, be scattered down by throwing to top, advance by setting path simultaneously.Skin in taking up the process of shedding in the tomato pomace and seed major part from.Tomato skin is easily dried and proportion is less, walks fast in hot blast, and drying time is short; Otherwise, tomato seed or skin seed grume be difficult do and proportion bigger, in hot blast, lose time, drying time is long.This drying machine is convenient to adjust the rotating cylinder rotating speed according to tomato pomace treating capacity, hot blast temperature and air quantity, can determine technological parameter by the operative employee according to the input and output material situation at any time.
Utilize the embedding skin seed of between drying machine discharging opening and terminal cleaner, connecting to rub discrete device afterwards, skin in the binding material fritter after the drying and seed are rubbed scattered, make the distinguished and admirable skin seed that has separated of carrying secretly enter the fractional sedimentation chamber, compartment of terrain, expansion chamber top is provided with plate washer, forces the landing of seed and skin bump.The cross section of expansion chamber makes wind speed gradually low after by forward direction.The volume leading portion part of expansion chamber is little, and back segment part is big, so that accept the tomato seed and the tomato skin of weight such as apparent gravity is different and basic respectively.
Isolated dry tomato skin improves density with the frame hydraulic press compression or with the granulation of ring mode comminutor, finishes pesticide-germicide simultaneously and improve density.
In to isolated tomato seed crude oil refining process, in order to keep beta carotene and the lycopene in the tomato seed oil, only it is carried out press filtration, comes unstuck and depickling, do not carry out decoloration and deodorization.To the tomato seed oil of transparent inner wrapping, take lucifuge trapping packing, as overcoat carton, dark plastic sheeting or aluminium-foil paper, and low temperature preserves, and prevents from that illumination and oxidation from causing to fade or rotten.
The invention has the advantages that: implementing the present invention can large-scale processing tomato skin seed slag, make the comprehensive utilization of tomato skin seed slag realize suitability for industrialized production, and water not in the technical process, not only significantly reduce the environmental pollution that wet tomato pomace itself causes, and eliminate the pollution of the high BOD that produces in the prior art wet separation skin seed technology and high suspended matter discharge of wastewater fully environment.
The specific embodiment:
Embodiment one: the tomato skin seed slag that goes the seed operation to discharge with the making beating of catsup factory is a raw material, adopts expeller to dewater in advance, makes its moisture content from more than 75%, drops to below 65%.Dehydration back wet feed enters the whizzer drying, and drying machine provides hot blast by coal-fired hot-blast stove.The rotating speed of whizzer is 0～10 rev/min of adjusting; Material is 30～50 minutes tube inner drying time, volume of material take up space volume 10%～20%/.Utilizing between drying machine discharging opening and terminal cleaner series connection to embed the skin seed then rubs discrete device and separates the skin seed, skin in the binding material fritter after the drying and seed are rubbed scattered, make the distinguished and admirable skin seed that has separated of carrying secretly enter the fractional sedimentation chamber, it is integrated to realize that the skin seed separates with drying process.It can be the pulverizer shape that the tomato skin seed is rubbed discrete device, but awl hits and hold in both hands or the sheet rotating speed is controlled at and makes the excellent sheet can complete centrifugal stretching, extension, is lower than 1400 rev/mins; Air inlet through hollow shaft and material, radially or tangential direction air-out and material; Charging can be enterprising formula, also can be side-feeding type.When the tomato skin of separating is made feed, tomato skin with the granulation of ring mode comminutor, is produced under the hot conditions at high pressure, make tomato skin finish the pesticide-germicide effect, make the apparent gravity of skin particle improve more than 5 times than diffusing shape dry hide.Make lycopene raw material etc. in particular cases in tomato skin, only use hydraulic press briquetting, not high pressure granulation.In the isolated tomato seed crude oil refining process,, only it is carried out press filtration, comes unstuck and depickling, do not carry out decoloration and deodorization in order to keep beta carotene and the lycopene in the tomato seed oil.To the tomato seed oil of transparent inner wrapping, take lucifuge trapping packing, as overcoat carton, dark plastic sheeting or aluminium-foil paper, and low temperature is preserved.
Embodiment two: compare with embodiment one, dewater in advance without expeller, and dewater with belt press.
Embodiment three: compare with embodiment one, tomato skin is used the hydraulic press briquetting without ring mode comminutor compressed granulate, or directly makes commodity selling.
Embodiment four: compare with embodiment one, the tomato seed does not extract grease and directly makes commodity selling.
Embodiment five: compare with embodiment one, the multicell expansion chamber changes tandem cyclone separator group into, and prime is isolated seed, and the back level is isolated skin.
Embodiment six: compares with embodiment one, and the embedding of between drying machine and skin seed expansion chamber, not connecting of skin seed discrete device, and be arranged in parallel with it.The skin seed compound that expansion chamber is collected when taking advantage of the drying machine shutdown, is sent into expansion chamber again and is isolated seed and skin after skin seed discrete device is handled.
Embodiment seven: compare with embodiment one, coal-fired hot-blast stove changes combustion gas or warm air oil furnace into.
Claims (2)
1. dehydrating with dry method skin seed discrete group combination production method of a catsup factory tomato skin seed slag is: the tomato skin seed slag that goes the seed operation to discharge with the making beating of catsup factory is a raw material, wet pelt seed slag is adopted the milling process dry skin seed that separates in back that dewaters in advance, skin improves density with compression and the high pressure-temperature pesticide-germicide is made particle, seed extracts tomato seed crude oil and oil meal with existing vegetable oil mill equipment and technology, it is characterized in that:
A, wet tomato skin seed slag adopt spiral squeezing dewatering machine to handle, and make its moisture content from dropping to more than 75% below 65%;
Skin seed slag after b, the processing adopts downflow type whizzer drying, and whizzer has three layers of rotating cylinder, and the rotating cylinder inwall all has the bowl-type flight of spiral layout, when drying machine rotates, material is taken up in the bottom, be scattered down by throwing, advance by setting path simultaneously to top;
C, connecting between drying machine discharging opening and terminal cleaner embeds the skin seed and rubs discrete device, and skin in the binding material fritter after the drying and seed are rubbed scattered;
D, the distinguished and admirable skin seed that has rubbed scattered of carrying secretly enter the fractional sedimentation chamber, and compartment of terrain, expansion chamber top is provided with plate washer, force the landing of seed and skin bump; The cross section of expansion chamber makes wind speed gradually low after by forward direction; The volume leading portion part of expansion chamber is little, and the back segment part is big, essentially identical tomato seed of weight and tomato skin so that accept the proportion difference respectively;
E, dry tomato skin improve density with the frame hydraulic press compression; Perhaps use the granulation of ring mode comminutor, finish pesticide-germicide simultaneously and improve density.
2. dehydrating and dry method skin seed discrete group combination production method by the described catsup of claim 1 factory tomato skin seed slag, it is characterized in that: tomato seed crude oil is only through carrying out press filtration, come unstuck and depickling it, do not decolour, the deodorization refining, tomato seed oil is adopted shading container and material packing.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2010101137855A CN101779775B (en) | 2010-02-25 | 2010-02-25 | Tomato skin, seed and residue dehydration drying and dry method skin and seed separation and combination production method in tomato paste factory |
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| Application Number | Priority Date | Filing Date | Title |
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| CN2010101137855A CN101779775B (en) | 2010-02-25 | 2010-02-25 | Tomato skin, seed and residue dehydration drying and dry method skin and seed separation and combination production method in tomato paste factory |
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| Publication Number | Publication Date |
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| CN101779775A CN101779775A (en) | 2010-07-21 |
| CN101779775B true CN101779775B (en) | 2011-12-07 |
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| CN2010101137855A Active CN101779775B (en) | 2010-02-25 | 2010-02-25 | Tomato skin, seed and residue dehydration drying and dry method skin and seed separation and combination production method in tomato paste factory |
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Families Citing this family (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US9434886B2 (en) * | 2011-12-31 | 2016-09-06 | Chenguang Biotech Group Co. Ltd. | Process for extracting lycopene |
| CN102687833A (en) * | 2012-06-14 | 2012-09-26 | 刘伯堂 | Method for producing tomato dietary fibers |
| CN102772339B (en) * | 2012-08-20 | 2013-11-27 | 刘伯堂 | Light-yellow transparent concentrated tomato waste liquid and preparation method and application thereof |
| CN103394468B (en) * | 2013-08-15 | 2015-09-02 | 新疆中聚粮油有限公司 | Impingement method seed skin separation method |
| CN112779082A (en) * | 2021-01-21 | 2021-05-11 | 四川俊文生态农业科技有限公司 | Peony seed oil processing and extracting method |
Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1142324A (en) * | 1996-05-27 | 1997-02-12 | 刘伯堂 | Production method for using peeling, seeds and residue from factory of tomato paste |
| CN1528184A (en) * | 2003-08-12 | 2004-09-15 | 傅敏恭 | Method for preparing paper-mouldtomato fiber food and use thereof |
| CN101148631A (en) * | 2007-11-09 | 2008-03-26 | 天津商业大学 | Method for preparing lycopene-enriched vegetable oil |
-
2010
- 2010-02-25 CN CN2010101137855A patent/CN101779775B/en active Active
Patent Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1142324A (en) * | 1996-05-27 | 1997-02-12 | 刘伯堂 | Production method for using peeling, seeds and residue from factory of tomato paste |
| CN1528184A (en) * | 2003-08-12 | 2004-09-15 | 傅敏恭 | Method for preparing paper-mouldtomato fiber food and use thereof |
| CN101148631A (en) * | 2007-11-09 | 2008-03-26 | 天津商业大学 | Method for preparing lycopene-enriched vegetable oil |
Non-Patent Citations (4)
| Title |
|---|
| 刘煜等.四号溶剂提取番茄籽油工艺和生产技术.《粮食与油脂》.2001,(第09期), * |
| 杨新辉等.番茄皮籽的回收利用研究进展.《食品工业科技》.2001,(第04期), * |
| 肖丽娟等.番茄籽油的性质及制取工艺.《粮油加工》.2006,(第01期), * |
| 董海洲等.番茄籽油的提取研究.《中国粮油学报》.2007,(第06期), * |
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Owner name: XINJIANG TUOMEITUO TOMATO SCIENCE + TECHNOLOGY DEV Effective date: 20120503 |
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Effective date of registration: 20120503 Address after: 831100 No. 6, science and technology Avenue, hi tech Industrial Development Zone, Xinjiang, Changji Patentee after: Xinjiang Tomatia Tomato Science & Technology Development Co., Ltd. Address before: The 1 group of 102488 Jiangxi province Jiujiang Jiujiang County min Shan Village Patentee before: Liu Botang |