CN1285161A - Tomato powder and production technology thereof - Google Patents
Tomato powder and production technology thereof Download PDFInfo
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- CN1285161A CN1285161A CN99117823A CN99117823A CN1285161A CN 1285161 A CN1285161 A CN 1285161A CN 99117823 A CN99117823 A CN 99117823A CN 99117823 A CN99117823 A CN 99117823A CN 1285161 A CN1285161 A CN 1285161A
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Abstract
The present invention relates to a tomato powder and its production process. It is characterized by diluting tomato paste and adopting spray-drying process to obtain tomato powder product whose appearance is made into granular form and partial powder form, possesses red colow, grain size is less than or equal to o.9 mm, density is 0.3-0.5 g/cu.cm, water content is less than or equal to 4%, acidity is less than or equal to 15%, total sugar is less than or equal to 50%, protein is greater than or equal to 10%, ash content is less than 10%, lead content is less than or equal to 1.0 mg/kg, arsenic content is less than or equal to 0.5 mg/kg and copper content is less than or equal to 10.0 mg/kg. It possesses good reconstituability, has no food additive and contains no pathogenic bacteria.
Description
Tomato meal of the present invention and production technology thereof relate to a kind of tomato product and preparation method thereof, especially a kind of tomato dry powder and preparation method thereof.
In the existing known technology is that the manufactured goods of raw material are based on catsup with the tomato, also have a small amount of tomato to do in addition, quick-frozen tomato etc., though there are potential needs in market to tomato meal, owing to fail to solve in the tomato meal production process difficult problem of sticking wall of slurry and bonding always, and actual development is not arranged, the production technology of catsup and equipment are all quite ripe in addition, and existing excess production capacity, can not obtain than good utilisation.
Goal of the invention of the present invention is to propose a kind of tomato powder product and is the production technology that raw material is produced this tomato meal with catsup.
Goal of the invention of the present invention is achieved through the following technical measures:
Tomato meal outward appearance of the present invention is fine granularity and part powdery, does not have caking, no solids, and no coke powder, color and luster are peony, redness, are mingled with few portion orange powder, and granularity≤0.9mm, 60-70% cross 60 mesh sieves, and density is 0.3-0.5g/cm
3, moisture≤4%, acidity≤15%, total reducing sugar≤50%, protein 〉=10%, ash content<10%, lead content≤1.0mg/kg, arsenic content≤0.5mg/kg, copper content≤10.0mg/kg, no food additives, total number of bacteria≤5000/g, coliform≤100/100g, saccharomycete≤500/100g, thunder bacterium≤50% in the positive visual field does not contain pathogenic bacteria.
Tomato meal of the present invention is raw material with catsup, to heat up 50~70 ℃ through running water batching diluted concentration 20~30% backs of sterilizing, filtering and disinfecting, slurry after the filtration atomizes under 1.1~1.9Mpa pressure, enter internal negative pressure and be-95~-drying tower of 185Pa in, through EAT is 200~250 ℃, leaving air temp is 85~110 ℃ of heated-air dryings, screening back packing.
Tomato meal of the present invention has reduced moisture and has not only prolonged the shelf-life effectively owing to adopt the drying one-tenth powder of catsup, and has significantly reduced the expense of packing and transportation.The loss of raw material nutrition is little, is a kind of good semi-finished product food.The production technology of catsup of the present invention can keep the nutritional labeling of product preferably, has kept original color and luster after the product rehydration substantially, has good rehydration.
Further specify below in conjunction with drawings and Examples:
Accompanying drawing 1 is the process flow diagram of tomato meal of the present invention and production technology thereof
Accompanying drawing 2 is process charts of the embodiment 5 of tomato meal of the present invention and production technology thereof
Embodiment 1: tomato meal fancy produce outward appearance of the present invention is fine granularity and small part powdery, does not have caking, no solids, and no coke powder, color and luster is peony, granularity<0.9mm, 100% crosses 20 orders, and 95% crosses 40 mesh sieves, and density is 0.45-0.5g/cm
3, moisture≤3%, acidity≤11%, total reducing sugar≤45%, protein 〉=12%, ash content<9%, lead content<0.5mg/kg, arsenic content<0.3mg/kg, copper content<5.0mg/kg, no food additives, total number of bacteria≤5000/g, coliform≤100/100g, saccharomycete≤500/100g, thunder bacterium≤50% in the positive visual field does not contain pathogenic bacteria.
Embodiment 2: tomato meal first class product appearance of the present invention is fine granularity and part powdery, does not have caking, no solids, and no coke powder, color and luster takes on a red color, the small part redness, granularity<0.9mm, 100% crosses 20 orders, and 95% crosses 40 mesh sieves, and density is 0.40-0.5g/cm
3, moisture≤4%, acidity≤13%, total reducing sugar≤50%, protein 〉=10%, ash content<11%, lead content<1.0mg/kg, arsenic content<0.5mg/kg, copper content<10.0mg/kg, no food additives, total number of bacteria≤5000/g, coliform≤100/100g, saccharomycete≤500/100g, thunder bacterium≤50% in the positive visual field does not contain pathogenic bacteria.
Embodiment 3: tomato meal of the present invention is raw material with catsup, to heat up 50~70 ℃ through running water batching diluted concentration 20~30% backs of sterilizing, filtering and disinfecting, slurry after the filtration atomizes under 1.1~1.9Mpa pressure, enter internal negative pressure and be-95~-drying tower of 185Pa in, through EAT is 200~250 ℃, leaving air temp is 85~110 ℃ of heated-air dryings, screening back packing.
Embodiment 4: the optimum working parameter scope of the production technology of tomato meal of the present invention is, with catsup is raw material, to heat up 65 ℃ ± 2 ℃ through running water batching diluted concentration 25 ± 0.1% backs of sterilizing, filtering and disinfecting, slurry after the filtration atomizes under 1.5Mpa ± 0.1Mpa pressure, enter in the drying tower of internal negative pressure for-150Pa ± 10Pa, through EAT is 230 ℃ ± 5 ℃, leaving air temp is 90 ℃ ± 5 ℃ heated-air dryings, screening back packing, technology is more stable under this scope, and product quality is higher.
Embodiment 5: catsup 4 is at room temperature added after blend tank 3 is 25% with the running water diluted concentration through sterilization and filtration by lifting device 2, be warming up under 70 ℃ and transport to duplex strainer 6 by feeding engine 5, catsup 4 slurries after filtering keep 70 ℃ through surge tank 7,25% concentration sprays into drying tower 11 by atomizer pump 8 from the top, 250 ℃ ± 10 ℃ the hot blast of being sent by hot-blast stove 19 is blown into drying tower 11 from the top with 230 ℃ of temperature, the lighter dry powder of a part is sent into cyclone separator 12 with 90 ℃ hot blast 9 from drying tower 11 middle parts, send into collector 14 by blower 10 along pipeline by the tomato meal that flow out drying tower 11 and cyclone separator 12 bottoms, finish packing by packing machine 13 at last.
Claims (7)
1. a tomato meal is characterized in that, outward appearance is fine granularity and part powdery, does not have caking, does not have
Solids, no coke powder, color and luster are peony, redness, are mingled with few portion orange powder, granularity≤
0.9mm 60-70% crosses 60 mesh sieves, density is 0.3-0.5g/cm
3, moisture≤4%,
Acidity≤15%, total reducing sugar≤50%, protein 〉=10%, ash content<10%, lead content≤
1.0mg/kg, arsenic content≤0.5mg/kg, copper content≤10.0mg/kg, no food additives,
Total number of bacteria≤5000/g, coliform≤100/100g, saccharomycete≤500/100g,
Thunder bacterium≤50% in the positive visual field does not contain pathogenic bacteria.
2. the production technology of a tomato meal is characterized in that, is raw material with catsup, sterilize to pass through,
Mistake is heated up 50~70 ℃ in running water batching diluted concentration 20~30% backs of filtering and disinfecting
Slurry after the filter atomizes under 1.1~1.9Mpa pressure, enters internal negative pressure for-95~185Pa's
In the drying tower, be 200~250 ℃ through EAT, leaving air temp is 85~110 ℃ of heated-air dryings,
Screening back packing.
3. tomato meal as claimed in claim 1 is characterized in that the fancy produce outward appearance is fine granularity
With the small part powdery, there is not caking, no solids, no coke powder, color and luster is peony, granularity<
0.9mm 100% crosses 20 orders, 95% crosses 40 mesh sieves, and density is 0.45-0.5g/cm
3,
Moisture≤3%, acidity≤11%, total reducing sugar≤45%, protein 〉=12%, ash content<9%,
Lead content<0.5mg/kg, arsenic content<0.3mg/kg, copper content<5.0mg/kg does not have food
The product additive, total number of bacteria≤5000/g, coliform≤100/100g, saccharomycete
≤ 500/100g, thunder bacterium≤50% in the positive visual field does not contain pathogenic bacteria.
4. tomato meal as claimed in claim 1 is characterized in that the first class product appearance is fine granularity
With the part powdery, there is not caking, no solids, no coke powder, color and luster takes on a red color, the small part redness,
Granularity<0.9mm, 100% crosses 20 orders, and 95% crosses 40 mesh sieves, and density is 0.40-
0.5g/cm
3, moisture≤4%, acidity≤13%, total reducing sugar≤50%, protein 〉=10%,
Ash content<11%, lead content<1.0mg/kg, arsenic content<0.5mg/kg, copper content<
10.0mg/kg, no food additives, total number of bacteria≤5000/g, coliform≤100
Individual/100g, saccharomycete≤500/100g, thunder bacterium≤50% in the positive visual field does not contain and causes
Germ.
5. the production technology of tomato meal as claimed in claim 2 is characterized in that, is former with catsup
Material is after the diluted concentration 20~30% of preparing burden through the running water of sterilizing, filtering and disinfecting
Heat up 50~70 ℃, the slurry after the filtration atomizes under 1.1~1.9Mpa pressure, enters inner negative
Press to-95~-drying tower of 185Pa in, be 200~250 ℃ through EAT, leaving air temp is
85~110 ℃ of heated-air dryings, screening back packing.
6. the production technology of tomato meal as claimed in claim 2 is characterized in that, optimum working parameter
Scope is, is raw material with catsup, to join through the running water of sterilizing, filtering and disinfecting
Heat up 65 ℃ ± 2 ℃ in material diluted concentration 25 ± 0.1% backs, the slurry after the filtration is at 1.5Mpa
± 0.1Mpa pressure is atomizing down, enters in the drying tower of internal negative pressure for-150Pa ± 10Pa warp
EAT is 230 ℃ ± 5 ℃, and leaving air temp is 90 ℃ ± 5 ℃ heated-air dryings, after the screening
Packing, technology is more stable under this scope, and product quality is higher.
7. the production technology of tomato meal as claimed in claim 2 is characterized in that, catsup (4) is by carrying
Rise device (2) and at room temperature add blend tank (3) with rare through the running water of sterilization and filtration
After releasing concentration and being 25%, be warming up under 70 ℃ and transport to duplex strainer (6), warp by feeding engine (5)
Catsup after the filtration (4) slurry keeps 70 ℃ through surge tank (7), and 25% concentration is by atomizer pump (8)
Spray into drying tower (11) from the top, 250 ℃ ± 10 ℃ the hot blast of sending by hot-blast stove (1) (9)
Be blown into drying tower (11) from the top with 230 ℃ of temperature, the lighter dry powder of a part is with 90 ℃ warm
Wind (9) is sent into cyclone separator (12) from drying tower (11) middle part, by drying tower (11) and cyclonic separation
The tomato meal that flow out device (12) bottom is sent into collector (14) by blower (10) along pipeline, at last by
Packing machine (13) is finished packing.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN99117823A CN1285161A (en) | 1999-08-21 | 1999-08-21 | Tomato powder and production technology thereof |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN99117823A CN1285161A (en) | 1999-08-21 | 1999-08-21 | Tomato powder and production technology thereof |
Publications (1)
Publication Number | Publication Date |
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CN1285161A true CN1285161A (en) | 2001-02-28 |
Family
ID=5280281
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
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CN99117823A Pending CN1285161A (en) | 1999-08-21 | 1999-08-21 | Tomato powder and production technology thereof |
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Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN103919067A (en) * | 2014-04-02 | 2014-07-16 | 浙江小二黑食品有限公司 | New method for preparing tomato powder |
CN104168776A (en) * | 2012-01-11 | 2014-11-26 | 哥伦比亚植物技术有限责任公司 | Dehydrated plant-derived products and methods for making the same |
-
1999
- 1999-08-21 CN CN99117823A patent/CN1285161A/en active Pending
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN104168776A (en) * | 2012-01-11 | 2014-11-26 | 哥伦比亚植物技术有限责任公司 | Dehydrated plant-derived products and methods for making the same |
CN103919067A (en) * | 2014-04-02 | 2014-07-16 | 浙江小二黑食品有限公司 | New method for preparing tomato powder |
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