CN105368708B - 一种卧式固体发酵系统 - Google Patents
一种卧式固体发酵系统 Download PDFInfo
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- CN105368708B CN105368708B CN201510736852.1A CN201510736852A CN105368708B CN 105368708 B CN105368708 B CN 105368708B CN 201510736852 A CN201510736852 A CN 201510736852A CN 105368708 B CN105368708 B CN 105368708B
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- 238000000855 fermentation Methods 0.000 title claims abstract description 49
- 230000004151 fermentation Effects 0.000 title claims abstract description 47
- 239000007787 solid Substances 0.000 title claims abstract description 27
- 239000000463 material Substances 0.000 claims abstract description 64
- 238000007599 discharging Methods 0.000 claims abstract description 28
- 238000003756 stirring Methods 0.000 claims abstract description 22
- 239000007788 liquid Substances 0.000 claims description 29
- 239000002699 waste material Substances 0.000 claims description 22
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances data:image/svg+xml;base64,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 data:image/svg+xml;base64,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 O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 13
- 238000011081 inoculation Methods 0.000 claims description 9
- OKTJSMMVPCPJKN-UHFFFAOYSA-N carbon Chemical compound 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[C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 8
- 229910052799 carbon Inorganic materials 0.000 claims description 8
- NBIIXXVUZAFLBC-UHFFFAOYSA-N phosphoric acid Chemical compound 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- 210000003128 Head Anatomy 0.000 description 1
- 210000000474 Heel Anatomy 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 238000010564 aerobic fermentation Methods 0.000 description 1
- LFVGISIMTYGQHF-UHFFFAOYSA-O azanium;phosphoric acid Chemical compound 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[P] OAICVXFJPJFONN-UHFFFAOYSA-N 0.000 description 1
- 229910052698 phosphorus Inorganic materials 0.000 description 1
- 239000011574 phosphorus Substances 0.000 description 1
- 238000007789 sealing Methods 0.000 description 1
- 231100000803 sterility Toxicity 0.000 description 1
- 239000012257 stirred material Substances 0.000 description 1
- 239000000758 substrate Substances 0.000 description 1
- 230000032258 transport Effects 0.000 description 1
- 230000000007 visual effect Effects 0.000 description 1
Classifications
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- C—CHEMISTRY; METALLURGY
- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12M—APPARATUS FOR ENZYMOLOGY OR MICROBIOLOGY; APPARATUS FOR CULTURING MICROORGANISMS FOR PRODUCING BIOMASS, FOR GROWING CELLS OR FOR OBTAINING FERMENTATION OR METABOLIC PRODUCTS, i.e. BIOREACTORS OR FERMENTERS
- C12M21/00—Bioreactors or fermenters specially adapted for specific uses
- C12M21/16—Solid state fermenters, e.g. for koji production
-
- C—CHEMISTRY; METALLURGY
- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12M—APPARATUS FOR ENZYMOLOGY OR MICROBIOLOGY; APPARATUS FOR CULTURING MICROORGANISMS FOR PRODUCING BIOMASS, FOR GROWING CELLS OR FOR OBTAINING FERMENTATION OR METABOLIC PRODUCTS, i.e. BIOREACTORS OR FERMENTERS
- C12M27/00—Means for mixing, agitating or circulating fluids in the vessel
- C12M27/02—Stirrer or mobile mixing elements
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- C—CHEMISTRY; METALLURGY
- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12M—APPARATUS FOR ENZYMOLOGY OR MICROBIOLOGY; APPARATUS FOR CULTURING MICROORGANISMS FOR PRODUCING BIOMASS, FOR GROWING CELLS OR FOR OBTAINING FERMENTATION OR METABOLIC PRODUCTS, i.e. BIOREACTORS OR FERMENTERS
- C12M29/00—Means for introduction, extraction or recirculation of materials, e.g. pumps
- C12M29/06—Nozzles; Sprayers; Spargers; Diffusers
-
- C—CHEMISTRY; METALLURGY
- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12M—APPARATUS FOR ENZYMOLOGY OR MICROBIOLOGY; APPARATUS FOR CULTURING MICROORGANISMS FOR PRODUCING BIOMASS, FOR GROWING CELLS OR FOR OBTAINING FERMENTATION OR METABOLIC PRODUCTS, i.e. BIOREACTORS OR FERMENTERS
- C12M41/00—Means for regulation, monitoring, measurement or control, e.g. flow regulation
- C12M41/12—Means for regulation, monitoring, measurement or control, e.g. flow regulation of temperature
- C12M41/18—Heat exchange systems, e.g. heat jackets or outer envelopes
- C12M41/20—Heat exchange systems, e.g. heat jackets or outer envelopes the heat transfer medium being a gas
-
- C—CHEMISTRY; METALLURGY
- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12M—APPARATUS FOR ENZYMOLOGY OR MICROBIOLOGY; APPARATUS FOR CULTURING MICROORGANISMS FOR PRODUCING BIOMASS, FOR GROWING CELLS OR FOR OBTAINING FERMENTATION OR METABOLIC PRODUCTS, i.e. BIOREACTORS OR FERMENTERS
- C12M41/00—Means for regulation, monitoring, measurement or control, e.g. flow regulation
- C12M41/40—Means for regulation, monitoring, measurement or control, e.g. flow regulation of pressure
Abstract
本发明涉及固体发酵技术领域，尤其涉及一种卧式固体发酵系统，包括卧式罐体、物料混合搅拌装置、动力装置、供气装置和卸料装置，物料混合搅拌装置设于卧式罐体内，且物料混合搅拌装置的一端与动力装置连接；卧式罐体的顶部设有入料口，卧式罐体的底部设有出料口，卧式罐体的一端设有进气口，另一端设有出气口；供气装置包括可控温空气发生器和鼓风机，可控温空气发生器的进气口与无菌空气压缩机连接，可控温空气发生器的出气口通过第一管道与第一进气口连接，鼓风机设于第一管道上，可控温空气发生器还包括循环气进口，循环气进口通过第二管道与第一出气口连接；卸料装置与出料口连接。能够快速调节发酵的物料达到合理的发酵温度。
Description
一种卧式固体发酵系统
技术领域
[0001] 本发明涉及固体发酵技术领域，尤其涉及一种卧式固体发酵系统。
背景技术
[0002] 固体发酵是指没有或几乎没有自由水存在下，在有一定湿度的水下溶性固态基质 中，用一种或多种微生物的一个生物反应过程。从生物反应过程中的本质考虑，固体发酵是 以气相为连续相的生物反应过程。固体发酵具有操作简便、能耗低、发酵过程容易控制、对 无菌要求相对较低、不易发生大面积的污染等优点。
[0003] 固体发酵在发酵时需要严格的控制发酵温度，目前，在固体发酵过程常采用水蒸 汽或热油对发酵物进行加热，采用冷水对发酵物进行降温，以保证发酵物在恒温条件下完 成发酵，但是采用水蒸汽为传热介质对发酵物进行加热时会导致物料水分不断增加、结团， 尤其是使面粉状物料结团后无法打散，造成罐内搅拌困难，物料不能均匀快速升温;使用热 油为热量传导工作介质，进行固体物料发酵灭菌时间长，能耗高、生产成本高，用冷水对发 酵物进行降温时降温较慢，不能快速让灭菌固体物料在实消后迅速达到恒温发酵温度。
发明内容
[0004] (一)要解决的技术问题
[0005] 本发明要解决的技术问题是解决现有技术中固体发酵系统难以实现恒温发酵的 问题。
[0006] (二)技术方案
[0007] 为了解决上述技术问题，本发明提供了一种卧式固体发酵系统，包括卧式罐体、物 料混合搅拌装置、动力装置、供气装置和卸料装置，所述物料混合搅拌装置设于所述卧式罐 体内，且所述物料混合搅拌装置的一端与动力装置连接;所述卧式罐体的顶部设有入料口， 所述卧式罐体的底部设有出料口，所述卧式罐体的一端设有进气口，另一端设有出气口；所 述供气装置包括可控温空气发生器和鼓风机，所述可控温空气发生器的进气口与无菌空气 压缩机连接，所述可控温空气发生器的出气口通过第一管道与所述第一进气口连接，所述 鼓风机设于所述第一管道上，所述可控温空气发生器还包括循环气进口，所述循环气进口 通过第二管道与所述第一出气口连接;所述卸料装置与所述出料口连接。
[0008] 其中，所述卧式罐体的侧壁包括内壁和外壁，所述内壁与所述外壁之间形成密闭 的空气隔层，所述外壁上设有第二进气口和第二出气口，且所述第二进气口、第二出气口分 别设于所述外壁的两端;所述第二进气口通过所述第一管道与所述可控温空气发生器的出 气口连接，所述第二出气口通过第二管道与所述循环气进口连接。
[0009] 其中，所述物料混合搅拌装置包括搅拌轴和螺带，所述螺带的数量为多对，每对所 述螺带以搅拌轴为中心相对设置，多对所述螺带的旋转直径均不相同；
[0010] 其中，所述搅拌轴贯穿于所述卧式罐体的两个端面，所述搅拌轴的内部设有空气 通道，且所述搅拌轴的一端与固定在所述卧式罐体的外侧的动力装置连接，另一端设有与 所述空气通道连通的第三进气口，所述第三进气口通过所述第一管道与所述可控温空气发 生器的出气口连接，且所述第三进气口处设有压力阀。
[0011] 其中，所述供气装置还包括储气罐、细菌过滤器和压力表，所述储气罐设于所述无 菌空气压缩机与所述可控温空气发生器之间，所述细菌过滤器和所述压力表设于所述第一 管道上，且所述细菌过滤器设于所述压力表和所述鼓风机之间。
[0012] 其中，还包括气液净化装置，所述气液净化装置包括净化箱和活性炭过滤器，所述 卧式罐体的侧壁的顶部设有排气口，所述卧式罐体的底部设有废液出口，所述排气口和所 述废液出口分别通过管道与所述净化箱连接，所述净化箱内设有磷酸溶液，用于吸收从排 气口排出的废气和从废液出口排出的废液，所述活性炭过滤器与所述净化箱通过管道连 接，用于进一步处理废气。
[0013] 其中，所述出料口设于所述卧式罐体的底部的中心位置处，所述出料口通过出料 管道与所述卸料装置连接，所述卸料装置由驱动电机带动。
[0014] 其中，所述卧式罐体上还设有温度测量口、压力测量口、取样口、接种口、备用气进 口和备用气出口，所述温度测量口和压力测量口分别用于测量所述卧式罐体内的温度和压 力，所述取样口、接种口分别用于对所述卧式罐体内的物料进行取样、接种，所述备用气进 口和所述备用气出口均设有压力阀。
[0015] 其中，所述外壁的底部设有冷凝水排出口和废液排净口，分别用于排出所述空气 隔层内的冷凝水和废液。
[0016] 其中，所述外壁的顶部还设有放空口，所述放空口处设有压力阀。
[0017] (三)有益效果
[0018] 本发明的上述技术方案具有如下优点：本发明的卧式罐体的一端设有第一进气 口，另一端设有第一出气口，当需要对卧式罐体内的发酵物进行加热时，与第一进气口连接 的可控温空气发生器将从无菌空气压缩机输出的空气加热到合适的温度，然后从第一进气 口通入到卧式罐体内，卧式罐体内的物料混合搅拌装置在对发酵物进行搅拌的过程中，使 发酵物和高温洁净的热空气与发酵物直接接触进行热传递，同样当需要对卧式罐体内的发 酵物进行降温时，可控温空气发生器向卧式罐体内通入冷空气，冷空气与发酵物直接接触 实现降温，利用空气对发酵物进行加热和降温，对发酵物不会造成污染，同时能够快速的使 发酵物达到要求的发酵温度，对物料进行灭菌，大大缩短了灭菌时间，同时完成热交换的热 空气或冷空气从第一出气口出来后再次进入到可控温空气发生器内，实现热、冷空气的循 环利用，节省了能耗，降低了生产成本。
附图说明
[0019] 图1是本发明实施例提供的卧式固体发酵系统的结构示意图。
[0020]图中：1:动力装置;2:物料混合搅拌装置;3:卧式罐体;4:卸料装置;5:旋转电机； 6:供气装置；10:驱动电机；11:减速器;21:搅拌轴;22:螺带;31:外壁;32:内壁;33:第一进 气口；34:第一出气口；35:第三进气口；％:接种口；37:排气口；38:放空口；39:压力测量口； 310:第二出气口； 311:废液出口； 312:冷凝水出口；313:备用气出口；314:备用气进口；315: 入料口；316:第二进气口；㈤:无菌空气压缩机;61:储气罐;62:可控温空气发生器;63:鼓风 机;64:细菌过滤器;65:压力表;7〇:第一主管;71:第一支管;72:第一支管;73:第一支管； 81:净化箱;82:活性炭过滤器;83:第二管道;84第二管道。
具体实施方式
[0021]为使本发明实施例的目的、技术方案和优点更加清楚，下面将结合本发明实施例 中的附图，对本发明实施例中的技术方案进行清楚、完整地描述，显然，所描述的实施例是 本发明的一部分实施例，而不是全部的实施例。基于本发明中的实施例，本领域普通技术人 员在没有做出创造性劳动的前提下所获得的所有其他实施例，都属于本发明保护的范围。 [0022]在本发明的描述中，需要说明的是，除非另有说明，“多个”的含义是两个或两个以 上;术语“上”、“下”、“左”、“右”、“内”、“外”、“前端”、“后端”、“头部”、“尾部”等指示的方位 或位置关系为基于附图所示的方位或位置关系，仅是为了便于描述本发明和简化描述，而 不是指示或暗示所指的装置或元件必须具有特定的方位、以特定的方位构造和操作，因此 不能理解为对本发明的限制。此外，术语“第一”、“第二”、“第三”等仅用于描述目的，而不能 理解为指示或暗示相对重要性。
[0023] 在本发明的描述中，还需要说明的是，除非另有明确的规定和限定，术语“安装”、 “相连”、“连接”应做广义理解，例如，可以是固定连接，也可以是可拆卸连接，或一体地连 接;可以是机械连接，也可以是电连接;可以是直接相连，也可以通过中间媒介间接相连。对 于本领域的普通技术人员而言，可视具体情况理解上述术语在本发明中的具体含义。
[0024]如图1所示，本发明实施例提供的一种卧式固体发酵系统，包括卧式罐体3、物料混 合搅拌装置2、动力装置1、供气装置6和卸料装置4，物料混合搅拌装置2设于卧式罐体3内， 且物料混合搅拌装置2的一端与动力装置1连接，动力装置1包括旋转电机10和与旋转电机 10连接的减速器11，物料混合搅拌装置2的左端通过联轴器与减速器11连接，卧式罐体3的 侧壁的顶部设有入料口 315，入料口 315的数量为两个，每个入料口 315处均设有与入料口 315密封连接的第二盖板，保证在发酵过程中罐体的密封。卧式罐体3的侧壁的底部设有出 料口，卸料装置4与出料口连接，卧式罐体3的一端的端面上设有第一进气口33，另一端的端 面上设有第一出气口 34;供气装置6包括可控温空气发生器62和鼓风机63，可控温空气发生 器62的进气口与无菌空气压缩机60连接，可控温空气发生器62的出气口通过第一管道与分 别与第一进气口 33和第二进气口连接，可控温空气发生器62的调节恒温热空气的温度范围 为17°_350°，调节恒温冷空气的温度范围为0°-16°，可控温空气发生器62还包括循环气进 口，循环气进口通过第二管道83与第一出气口 34连接。
[0025]对固体进行发酵时，将固体物料从入料口315加入到卧式罐体3内，启动动力装置1 带动物料混合搅拌装置2对物料进行搅拌，当需要调整发酵温度时，无菌空气压缩机60开始 工作，将无菌压缩空气输入到可控温空气发生器62对压缩空气进行加热或降温，当需要升 高卧式罐内的温度时，从第一进气口 33向卧式罐体3内输入高温的洁净热空气，热空气进入 到卧式罐体3后与进行搅拌的物料直接充分的接触，实现热空气与物料的换热，从而使物料 快速达到合适的发酵温度，当需要降低卧式罐体3内的温度时，从第一进气口 33向卧式罐体 3内输入冷空气，冷空气与物料直接接触换热，对卧式罐体3内的物料进行降温，从而能达到 合适的发酵温度。并且与物料完成和交换的空气从卧式罐体3底部的第一出气口 34出来，经 第二管道83从循环进气口再次进入到可控温空气发生器62，实现空气的循环利用，具有采 用空气换热的方式，一次可发酵1吨至2吨的固体物料，且具有换热快，并热交换快，能够快 速升温进行物料灭菌，缩短物料灭菌时间，增加设备生产量、节省能耗、降低生产成本，满足 大量固体物料发酵需求，同时实现了空气的循环利用。
[0026]卧式罐体3的侧壁包括内壁32和外壁31，内壁32与外壁31均为圆筒形，且内壁32与 外壁31之间形成密闭的空气隔层，外壁31的一端设有第二进气口 316,外壁31的另一端设有 第二出气口310,且第二进气口 316和第二出气口 310设于外壁w的两端成对角设置;第二进 气口316通过第一管道与可控温空气发生器62的出气口连接，第二出气口 310通过第二管道 84与循环气进口连接。从可控温空气发生器62出来的热空气或冷空气进入到空气隔层后与 物料间接接触，因此可以实现物料的无氧发酵，空气隔层中与物料完成热交换的热空气或 冷空气从第二出气口 310出来后再次进入到可控温空气发生器62,实现空气的循环利用，完 成发酵后的物料从出料口进入到卸料装置4进行卸料。
[0027]该系统中的物料混合搅拌装置2包括搅拌轴21和螺带22,螺带22的数量为多对，每 对螺带22以搅拌轴21为中心相对设置，多对螺带22的旋转直径均不相同，多对螺带22之间 通过固定杆固定，固定杆穿过搅拌轴21，每对螺带22均关于固定杆对称，且固定在固定杆 上，在搅拌轴21的两侧均形成多层螺带22,一般采用2层或3层，在本实施例中，共有2对螺带 22,也就是在搅拌轴21的两侧均有2层螺带22,其中外层螺带将物料从两侧向中央汇集，内 层螺带将物料从中央向两侧输送，使物料在流动过程中形成更多的涡流，形成一个低动力 高效的混合环境，使物料的混合均匀度高，混合速度快，效率高，能耗低，且混合过程温和， 基本不会破坏物料的原始状，对物料无污染。
[0028]搅拌轴21贯穿于卧式罐体3的两个端面之间，搅拌轴21的一端与设于卧式罐体3的 外侧的动力装置1连接，搅拌轴21内设有空气通道，搅拌轴21的另一端设有与空气通道连通 的第三进气口 35，第三进气口 35通过第一管道与可控温空气发生器62的出气口连接，可控 温空气发生器62内的热空气或冷空气进入到空气通道中，与卧式罐体3内的物料进行热交 换，第三进气口3f5处设有压力阀，当空气通道内的压力过大时，压力阀打开，气体从第二进 气口 3ie出来，缓解空气通道内的压力，保证安全性；其中，第一管道包括第一主管70和支 管，第一主管70的数量为一个，支管的数量为三个，包括第一支管71、第一支管72和第一支 管73,第一支管H与第一进气口 33连接，第一支管72与第二进气口连接，第三支管73与第三 进气口 35连接，第一主管70与可控温空气发生器62的出气口连接。三个第一支管上均设有 阀门，阀门的开闭控制可控温空气发生器62内出来的热空气或冷空气进入到卧式罐体3内 部、空气隔层或空气通道内，当从可控温空气发生器62内的出来的热空气或冷空气时进入 到空气隔层或空气通道时，热空气或冷空气与物料发生间接换热，实现卧式罐体3内的物料 的无氧发酵，当从可控温空气发生器62内的出来的热空气或冷空气时进入内壁32时，热空 气或冷空气与正在搅拌的物料直接充分接触换热速度更快，同时通入到内壁32内的热空气 或冷空气中的氧气为物料的有氧发酵提供了条件。
[0029]供气装置6还包括储气罐61、细菌过滤器64和压力表65，储气罐61设于无菌空气压 缩机6〇与温空气发生器之间，储气罐61将无菌空气压缩机60内生成的无菌压缩空气进行储 存，细菌过滤器64和压力表65设于第一主管70上，且细菌过滤器64设于压力表65和鼓风机 63之间，细菌过滤器64对从可控温空气发生器62内输出的空气进行过滤，避免空气中的杂 质对卧式罐体3内的物料造成污染，压力表65用来检测进入卧式罐体3的空气的压力，根据 压力表65检测的压力，无菌空气压缩机60合理的调整空气的压力。
[0030]还包括气液净化装置，气液净化装置包括净化箱81和活性炭过滤器84,卧式罐体3 的侧壁的顶部设有排气口 37，卧式罐体3的侧壁底部设有废液出口 311，排气口 37和废液出 口 311分别通过气体管道和液体管道与净化箱81连接，其中排气口 37通过气体管道与净化 箱81的进气口连接，废液出口 ：311通过液体通道与净化箱81的进液口连接，净化箱81内设有 磷酸溶液，用于吸收从排气口 37排出的废气和从废液出口 311排出的废液，从排气口 37排出 的发酵废气和从废液出口 311排出的废液进入到净化箱81后与磷酸溶液反应，转换成磷酸 铵肥料，供农作物生长使用，即节能环保又彻底解决了排出物的污染问题，活性炭过滤器84 通过气体管道与净化箱81的出气口连接，对从净化箱81内排出的废气进一步进行处理，然 后排到空气中，避免污染空气。
[0031]出料口设于卧式罐体3的底部的中心位置处，出料口通过出料管道与卸料装置4连 接，卸料装置4由驱动电机带动。如图1所示，卧式罐体3内完成发酵的物料经从出料口经出 料管道进入到卸料装置4的左端，卸料装置4的内部设有螺杆，螺杆由驱动电机带动旋转，螺 杆在旋转过程中，带着物料向卸料装置4的右端运输，从右侧底部的出口进行卸料。卸料装 置4包括粉体球面阀或梅花错位阀，粉体球面阀可以最大程度的减小搅拌死角，并实现最大 口径的放料口面积;梅花错位阀可实现简单操作和控制放料速度，并可组合长螺旋底部支 撑装置，阀门的驱动可采用手动、气动和电动三种。
[0032]卧式罐体3上设有温度测量口、压力测量口 39、取样口、接种口 36、备用气进口 314 和备用气出口 313,温度测量口 317和压力测量口⑽分别用于测量卧式罐体3内的温度和压 力，根据检测到的卧式罐体3内的温度及压力进行调整，保证卧式罐体3内的压力和温度在 合适的范围内。取样口、接种口 36分别用于对卧式罐体3内的物料进行取样和接种，当完成 取样和接种后要将取样口和接种口 36密封，保证发酵环境的密封性，备用气进口 314和备用 气出口 313均设有压力阀。当卧式罐体3内的压力值超过卧式罐体3的最大压力承受值时，备 用气进口 314和备用气出口 313的压力阀打开，卧式罐体3内的气体从备用气进口 314或备用 气出口 313排出，缓解卧式罐体3内的压力值，保证安全的发酵的环境;外壁31的底部设有冷 凝水出口312和废液排净口，分别用于排出空气隔层内的冷凝水和废液。
[0033]外壁31上还设有放空口 38,放空口 38处设有压力阀，当空气隔层内的压力值大于 其能承受的最大值时，放空口 38处的压力阀打开，缓解空气隔层内的压力，保证安全的工作 环境。
[0034]另外，本发明的卧式罐体3内的物料在发酵时含有一定的水分，可以使在上料、混 合和出料过程中均无粉尘飞扬，较为环保，不会造成对周围环境的破坏。
[0035]使用时，将供气装置6通过第一管道分别与第一进气口 33、第二进气口 316和第三 进气口 35连接，根据在温度检测口检测到的卧式罐体3内的温度向卧式罐体3、空气隔层和 空气通道中通入高温空气或冷空气，通过物料混合搅拌装置2对物料进行混合搅拌，从而使 进入到卧式罐体3内的高温空气或冷空气与物料充分直接接触，完成直接换热，同时进入到 空气隔层和空气通道内的高温空气或冷空气与卧式罐体3内的物料进行间壁式换热，进一 步提高换热速度，换热后的空气从卧式罐体3的一个端面、外侧壁的底部排出再次进入到供 气装置6中，实现资源的循环利用。发酵生成的废气通入到气液净化装置的净化箱81内的磷 酸溶液发生反应生成磷酸铵肥料，用于农作物生长，反应后的气体经活性炭过滤器82后排 出，既环保又解决了排出物的污染问题。完成发酵的物料从卧式罐体3底部的出料口进入到 「mir ^枓在发酵过程中需要不断的往卧式罐体3内补充无菌水分。 、紐®发明的卧式固体发酵系统通过向卧式罐体内的发酵的物料通入满足 触混合换热和间壁式换热两种方式，实现对卧式罐体内发酵温 度的快速调节，且干净无污染，解决了现有技术中以水蒸汽、热油和冷水做换热介质造成的 物料难以搅拌和很难达到发酵温度的问题。
[0037]最后应说明的是:以上实施例仅用以说明本发明的技术方案，而非对其限制;尽管 参照前述实施例对本发明进行了详细的说明，本领域的普通技术人员应当理解:其依然可 以对前述各实施例所记载的技术方案进行修改，或者对其中部分技术特征进行等同替换； 而这些修改或者替换，并不使相应技术方案的本质脱尚本发明各实施例技术方案的精神和 范围。
Claims (9)
1. 一种卧式固体发酵系统，其特征在于:包括卧式罐体、物料混合搅拌装置、动力装置、 供气装置和卸料装置，所述物料混合搅拌装置设于所述卧式罐体内，且所述物料混合搅拌 装置的一端与动力装置连接;所述卧式罐体的顶部设有入料口，所述卧式罐体的底部设有 出料口，所述卧式罐体的一端设有第一进气口，另一端设有第一出气口；所述供气装置包括 可控温空气发生器和鼓风机，所述可控温空气发生器的进气口与无菌空气压缩机连接，所 述可控温空气发生器的出气口通过第一管道与所述第一进气口连接，所述鼓风机设于所述 第一管道上，所述可控温空气发生器还包括循环气进口，所述循环气进口通过第二管道与 所述第一出气口连接;所述卸料装置与所述出料口连接;所述物料混合搅拌装置包括搅拌 轴和螺带;所述搅拌轴贯穿于所述卧式罐体的两个端面，所述搅拌轴的内部设有空气通道， 且所述搅拌轴的一端与固定在所述卧式罐体的外侧的动力装置连接，另一端设有与所述空 气通道连通的第三进气口，所述第三进气口通过所述第一管道与所述可控温空气发生器的 出气口连接，且所述第三进气口处设有压力阀。
2. 根据权利要求1所述的卧式固体发酵系统，其特征在于:所述卧式罐体的侧壁包括内 壁和外壁，所述内壁与所述外壁之间形成密闭的空气隔层，所述外壁上设有第二进气口和 第二出气口，且所述第二进气口、第二出气口分别设于所述外壁的两端;所述第二进气口通 过所述第一管道与所述可控温空气发生器的出气口连接，所述第二出气口通过第二管道与 所述循环气进口连接。
3. 根据权利要求1所述的卧式固体发酵系统，其特征在于:所述螺带的数量为多对，每 对所述螺带以搅拌轴为中心相对设置，多对所述螺带的旋转直径均不相同。
4. 根据权利要求1所述的卧式固体发酵系统，其特征在于：所述供气装置还包括储气 罐、细菌过滤器和压力表，所述储气罐设于所述无菌空气压缩机与所述可控温空气发生器 之间，所述细菌过滤器和所述压力表设于所述第一管道上，且所述细菌过滤器设于所述压 力表和所述鼓风机之间。
5. 根据权利要求1所述的卧式固体发酵系统，其特征在于:还包括气液净化装置，所述 气液净化装置包括净化箱和活性炭过滤器，所述卧式罐体的侧壁的顶部设有排气口，所述 卧式罐体的底部设有废液出口，所述排气口和废液出口分别通过管道与所述净化箱连接， 所述净化箱内设有磷酸溶液，用于吸收从排气口排出的废气和从废液出口排出的废液，所 述活性炭过滤器与所述净化箱通过管道连接，用于进一步处理废气。
6. 根据权利要求1所述的卧式固体发酵系统，其特征在于:所述出料口设于所述卧式罐 体的底部的中心位置处，所述出料口通过出料管道与所述卸料装置连接，所述卸料装置由 驱动电机带动。
7. 根据权利要求1所述的卧式固体发酵系统，其特征在于:所述卧式罐体上还设有温度 测量口、压力测量口、取样口、接种口、备用气进口和备用气出口，所述温度测量口和压力测 量口分别用于测量所述卧式罐体内的温度和压力，所述取样口、接种口分别用于对所述卧 式罐体内的物料进行取样、接种，所述备用气进口和所述备用气出口均设有压力阀。
8. 根据权利要求2所述的卧式固体发酵系统，其特征在于:所述外壁的底部设有冷凝水 排出口和废液排净口，分别用于排出所述空气隔层内的冷凝水和废液。
9. 根据权利要求2所述的卧式固体发酵系统，其特征在于:所述外壁的顶部还设有放全 口，所述放空口处设有压力阀。
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