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蒸汽喷射蒸煮器将所有蒸汽能量无损地转化为液体，可立即液化您的加工物料，并最大限度地提高效率。

高效喷射器

喷射器.png

Changcheng - Turnkey

Changcheng - Turnkey

Changcheng - Turnkey

设备

Model
Capacity (m³/h starch slurry)
Steam Consumption (kg/h)
Steam Pressure (bar)
Nozzle Ø (mm)
Mixing Tube Length (mm)
Material
Control Mode
SCCB-03
3 – 5
150 – 250
2 – 3
2.5
300
SS 316L
Automatic / Manual
SCCB-06
6 – 10
300 – 450
2 – 3
3.5
350
SS 316L
Automatic / Manual
SCCB-10
10 – 15
500 – 700
2 – 4
4.5
400
SS 316L
Automatic / Manual
SCCB-15
15 – 20
750 – 950
2 – 4
5.5
450
SS 316L
Automatic / Manual
SCCB-20
20 – 30
1 000 – 1 300
2 – 4
6.5
500
SS 316L
Automatic / Manual
SCCB-30
30 – 40
1 400 – 1 800
2 – 4
8
550
SS 316L
Automatic / Manual
SCCB-40
40 – 50
1 900 – 2 300
2 – 4
9
600
SS 316L
Automatic / Manual
SCCB-50
50 – 60
2 400 – 2 800
2 – 5
10
650
SS 316L
Automatic / Manual
SCCB-80
60 – 80
3 000 – 3 600
2 – 5
12
700
SS 316L
Automatic / Manual
SCCB-100
80 – 120
4 000 – 5 000
2 – 5
15
800
SS 316L
Automatic / Manual

概述
SCCB 系列全自动液化喷射器专为各种液化应用而设计，尤其适用于糖浆和淀粉糖生产线。其设计消除了任何易腐蚀或堵塞的部件，确保连续不间断运行。强烈的湍流可瞬间混合蒸汽和液体，加速并简化液化过程，使后续生产步骤顺利进行。尽管体积小巧，但这些喷射器在淀粉糖加工生产线中仍能提供卓越的效率。​

 

主要特点

  • 即时、静音传热：蒸汽的显热和潜热直接注入液体，不会产生振动或巨大的“蒸汽锤”噪音。​

  • 精确的蒸汽流量控制：通过调节蒸汽阀杆和喷嘴之间的横截面积，可以精细、逐步地调节出口温度。​

  • 无振动混合：混合管运行时不会产生振动，并可同时调节压力和流量。​

  • 即时温度响应：传热过程无障碍或滞后；控制系统可将出口温度保持在±1°C以内。​

  • 接近100%的热效率：蒸汽的显热和潜热均完全传递给液体，实现几乎无损耗的热交换。

​​

工作原理
SCCB系列喷射器采用接触式蒸汽喷射进行液化。高压蒸汽进入喷射器主体，并通过喷嘴喷出进入混合管，在强烈的湍流作用下与液体相遇。这确保了蒸汽与液体之间的瞬时热传递，几乎没有能量损失，从而快速达到所需的出口温度。​

  • 出口温度控制：通过调节阀杆和喷嘴之间的间隙来调节蒸汽流量，可直接调节出口温度。​

  • 流量调节：混合管轴向运动可调节液体管路压力和流量。​

  • 不间断运行：内部流道可防止堵塞，减震安装设计可延长维护间隔并降低停机风险。

Product
Jet Cooker Application
Ethanol (Ethyl Alcohol)
Used for the primary liquefaction of corn, wheat, or rye mash; the slurry is passed through the jet cooker at 221 °F (105 °C) for 5 minutes, then held at 180–190 °F (82–88 °C) for 1–2 hours prior to enzymatic processing.
Corn Starch
Used in wet milling processes for gelatinization and liquefaction of starch slurry; controlled heating between 160–300 °F (71–149 °C) and high-turbulence mixing to solubilize the starch.
Wheat Starch
Used for hydrothermal liquefaction of wheat starch; provides homogeneous heating and continuous flow before enzymatic hydrolysis for efficient conversion.
Citric Acid
Used to continuously sterilize and heat fermentation media; direct steam injection via the jet cooker enables short-duration (flash) high-temperature sterilization.
Xanthan Gum
Used to heat fermentation media before inoculation and to heat polymer solutions post-fermentation; high-shear, turbulent mixing ensures homogeneous viscosity control and particle dispersion.
Lysine
Used to heat and sterilize amino acid fermentation media; rapid heating via the jet cooker reduces infection risk and the medium is fed directly into the fermenter.
Sorbitol
Used to liquefy and gelatinize starch-based glucose syrups prior to hydrogenation; pre-heats the syrup with the jet cooker to produce a low-viscosity feedstock ready for enzymatic hydrolysis.
Maltodextrin
Used for primary liquefaction of starch syrups in maltodextrin production; controlled heating and continuous mixing yield a homogeneous syrup with low dextrose equivalent (DE).
Modified Starch
Used as a pre-treatment for starch granule disruption and to increase reactive group accessibility; the jet cooker provides controlled thermal and mechanical action.
Maltose/Dextrose Syrup
Used for liquefying starch solutions prior to saccharification; the jet-cooked syrup is prepared for enzyme reactions.
Lactic Acid
Used to heat and sterilize lactic acid fermentation media; the jet cooker supplies a sterilized, heated medium directly to the fermenter.
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