固定化培养和产物释放促进剂对硬紫草细胞代谢的影响

固定化培养的硬紫草细胞生长缓慢,仅包理球外层的细胞生长明显,其蛋白质合成的量也低。培养３０ｄ的细胞色素产量达到４．２ｍｇ／ｇＦＷ,相对色素分泌量达到７０％,而色素的组成成分及各组分的比例也与悬浮细胞的不同。以正十六烷处理固定化细胞可促进产物释放,其不同的处理时间对细胞没有显著影响。连续培养的固定细胞保持其色素形成能力达８０ｄ之久,色素总产量达２０ｍｇ／ｇＦＷ．     

γ—射线对滇紫草细胞产生色素的影响

应用５００～２５００伦琴（Ｒ）的６０钴γ射线照射滇紫草（ＯｎｏｓｍａｐａｎｉｃｕｌａｔｕｍＢｕｒ．ｅｔＦｒａｎｃｈ．）细胞系,确定了应用γ射线处理促进紫草素合成的最适辐照剂量为１５００Ｒ,处理后的细胞系在生产培养基上培养２１ｄ后紫草素含量（以干重计）达到９４．７９ｍｇ／ｇ,较对照提高了１４４６％,通过小团块选种法从中筛选到了色素含量（以干重计）高达１０３．４２ｍｇ／ｇ的高产细胞系Ｍｕｔ１,其营养生长与对照相比没有差别。     

真菌诱导物在滇紫草细胞培养中对紫草色素形成的影响

在滇紫草细胞悬浮培养中,真菌诱导物可抑制细胞生长,促进草色素的合成,将培养６ｄ的曲霉菌丝体的粗提物以６００μｇ碳水化合物／５０ｍｌ培养液的浓度加入到处于指数生长初期的滇紫草细胞悬浮培养物中,诱导物促进紫草色素合成的作用最大,紫草色素含量为对照的两倍,经高压锅处理２０ｍｉｎ到２ｈ不影响诱导物的活性,真菌诱导物还影响了紫草色素各衍生物的相对含量。     

硬紫草悬浮细胞原生质体培养形成愈伤组织及其体细胞克隆变异

从硬紫草悬浮细胞系ＡＲ１２６分离原生质体,只有用葡萄糖作渗透剂经琼脂糖－液体双层培养才能获得可见的原生质体克隆,从中选择３４个克隆,用两阶段法生产紫草素及其衍生物,测量了它们在两阶段的细胞生长量及生产阶段的色素含量,并比较了其分布规律,其中最好的原生质体克隆色素生产量是起始悬浮系的２．５４倍,经培养４０ｄ达４４．０６ｍｇｇ－１ＦＷ,而且其生产量在所测的８０ｄ内无明显下降。     

真菌诱导物在滇紫草细胞培养中对紫草色素形成的影响

在滇紫草细胞悬浮培养中,真菌诱导物可抑制细胞生长,促进紫草色素的合成。将培养６ｄ的曲霉菌丝体的粗提物以６００μｇ碳水化合物／５０ｍｌ培养液的浓度加入到处于指数生长初期的滇紫草细胞悬浮培养物中,诱导物促进紫草色素合成的作用最大,紫草色素含量为对照的两倍。经高压锅处理２０ｍｉｎ到２ｈ不影响诱导物的活性。真菌诱导物还影响了紫草色素各衍生物的相对含量。     

用无血清培养基在填充床生物反应器生产 rHuEPO

在填充床生物反应器用含５％ＦＢＳ的ＤＭＥＭ：Ｆ１２培养基培养产重组人促红细胞生成素（ｒＨｕＥＰＯ）的细胞Ｃ_２８～１０ｄ后,使用自制的无血清生产培养基（ＳＦＭｐ）生产ｒＨｕＥＰＯ。ＳＦＭｐ培养基既能维持细胞生长,又能生产ＥＰＯ,也便于纯化分离ｒＨｕＥＰＯ。使用填充床生物反应器培养细胞,能维持培养２０～２５ｄ,ｒＨｕＥＰＯ表达水平达１２～２８.４ｍｇ／Ｌ之间,反应器的产率达到７１.０ｍｇ／Ｌ／ｄ,比滚瓶的产率增加１２～１４倍。葡萄糖最高消耗量达到２１ｇ／Ｌ／ｄ,细胞培养密度最高达到３.０×１０^７／ｍｌ以上,每次可收无血清培养上清８０～８７Ｌ。由于细胞被固定在聚酯片上,培养上清中脱落细胞很少。观察了反应器的乳酸和氨的含量,其结果表明乳酸和氨含量分别低于３.５ｇ／Ｌ和５ｍｍｏｌ／Ｌ,不影响产物的表达。经过多批培养和生长ｒＨｕＥＰＯ的结果表明,自行配制的ＳＦＭｐ培养基在该反应器能有效地维持细胞生长和生产ｒＨｕＥＰＯ。     

用无血清培养基在填充床生物反应生产rHuEPO

在填充床生物反应器用含５％ＦＢＳ的ＤＭＥＭ：Ｆ１２培养基培养产重组人促红细胞生成素（ｒＨｕＥＰＯ）的细胞Ｃ２８￣１０ｄ后,使用自制的无血清生产培养基（ＳＦＭ－ｐ）生产ｒＨｕＥＰＯ。ＳＦＭ－ｐ培养基既能维持细胞生长,又能生产ＥＰＯ,也便于纯化分离ｒＨｕＥＰＯ。使用填充床生物反应器培养细胞,能维持培养２０￣２５ｄ,ｒＨｕＥＰＯ表达水平达１２￣２８．４ｍｇ／Ｌ之间,反应器的产率达到７１．０ｍｇ／Ｌ／ｄ,     

利用高山红景天培养细胞生物转化外源酪醇生产红景天甙的研究

高山红景天（ＲｈｏｄｉｏｌａｓａｃｈａｌｉｎｅｎｓｉｓＡ．Ｂｏｒ．）培养细胞中,甙元酪醇在细胞生长静止期大量积累,而此时糖基化反应的效率很低,因而红景天甙（ｓａｌｉｄｒｏｓｉｄｅ）产量较低。考虑到培养细胞中酪醇葡萄糖基转移酶的活性在指数生长期达到最高,考察了在指数生长期添加外源酪醇生物转化生产红景天甙的可能性,并探讨了酪醇添加浓度、添加方法及细胞密度对酪醇转化率及红景天甙产量的影响。结果表明,细胞在酪醇浓度为１ｍｍｏｌ／Ｌ的培养基中培养２４ｈ后可使酪醇转化率达到９５％;过高的酪醇浓度（＞３ｍｍｏｌ／Ｌ）对细胞生长及酪醇转化率都有明显抑制作用;通过较低浓度酪醇的３次重复添加,可使细胞密度为６ｇＤＷ／Ｌ、１２ｇＤＷ／Ｌ及１８ｇＤＷ／Ｌ的培养物中的红景天甙产量分别达到１３２０ｍｇ／Ｌ、１７４０ｍｇ／Ｌ和１９８０ｍｇ／Ｌ。     

水母雪莲悬浮培养细胞生长和黄酮类活生成分合成

在ＭＳ培养基上进行水母雪莲细胞悬浮培养,研究了摇床转速、接种量、培养液初始ｐＨ、碳源等的影响。结果表明,摇床转速为９０￣１２０ｒ／ｍｉｎ,接种量为５０￣８０ｇＦＷ／Ｌ,培养液初始ｐＨ５．５￣６．０,对水母雪莲悬浮培养细胞生长和黄酮合成最有利。碳源以蔗糖最适合,蔗糖浓度则以４０ｇ／Ｌ较好,此时细胞生长量为１８￣１９ｇＤＷ／Ｌ,总黄酮合成量可达１４２３．２５ｍｇ／Ｌ。用ＨＰＬＣ检测显示４＇,５,７－三     

黄花蒿培养细胞中青蒿素合成代谢的体外调节

黄花蒿培养细胞通过两步培养积累青蒿素．第１步在含有０．２～０．４ｍｇ／Ｌ６－苄基氨基嘌呤（６－ＢＡ）和３～４ｍｇ／Ｌ吲哚乙酸（ＩＡＡ）的Ｎ６培养基中进行细胞的增殖培养,第２步将培养好的细胞转入含０．２～０．４ｍｇ／Ｌ６－ＢＡ和０．２～０．４ｍｇ／ＬＩＡＡ的改良Ｎ６培养基中进行青蒿素的合成．青蒿素的合成量为１９０μｇ／ｇ干细胞左右．当在第２步培养中加入青蒿素合成前体青蒿酸,青蒿素合成量比仅靠激素诱导提高了３倍多．青蒿素的合成途径是植物固醇合成途径的分支途径,当在青蒿素合成过程即第２步培养中加入固醇生物合成抑制剂双氯苯咪唑和氯化氯胆碱处理,可使代谢向合成青蒿素的方向移动,青蒿素合成量明显提高．经２００ｍｇ／Ｌ氯化氯胆碱处理２ｄ,黄花蒿细胞合成青蒿素量为３７２μｇ／ｇ干细胞;经２０ｍｇ／Ｌ双氯苯咪唑处理４ｄ,黄花蒿细胞合成青蒿素量为１５４０μｇ／ｇ干细胞,比靠激素诱导提高了８倍多,与诱导脱分化细胞的黄花蒿叶中所含的青蒿素（３０００μｇ／ｇ干细胞）处于同一个数量级．以上结果表明：在通过植物激素调节可以合成青蒿素的黄花蒿培养细胞中,缺乏青蒿素合成前体是青蒿素合成量低的重要原因．因此,在青蒿素合成的过程中通过体外调节,     

Physico-chemical factors influencing the shikonin derivatives production in cell suspension cultures of Arnebia euchroma (Royle) Johnston, a medicinally important plant species

Cell suspension cultures of Arnebia euchroma were raised from in vitro leaf-derived friable callus on liquid MS [Murashige and Skoog] medium supplemented with BAP (6-benzylaminopurine) (10.0 μM) and IBA (indole-3-butyric acid) (5.0 μM). A two-stage culture system was employed using growth and production medium for cell biomass and shikonin derivatives, respectively. Factors such as light, temperature, sucrose and pH (hydrogen ion concentration) were studied to observe their effect on the shikonin derivative production. Light conditions completely inhibited shikonin derivative production. Out of different temperature regimes tested, the highest yield (586.17 μg/g FW) was found at 25°C. Maximum production (656.14 μg/g FW) was observed in 6% sucrose. An alkaline pH (7.25-9.50) favoured shikonin derivative production. The results showed that physical and chemical factors greatly influence the production of shikonin derivatives in cell suspension cultures of A. euchroma. Therefore, by employing optimum culture conditions, it is possible to enhance the production of secondary compounds from the cells. The factors optimized for in vitro production of shikonin derivatives during the present study can successfully be employed for their large-scale production in bioreactors.     

pH值、激素对新疆紫草悬浮培养细胞生长及紫草宁衍生物合成的影响

报道了不同ｐＨ值、激素对新疆紫草悬浮培养细胞生长及紫草宁衍生物合成的影响。结果表明,新疆紫草细胞具有自我调节其培养液ｐＨ值的功能。适合于细胞生长及紫草宁衍生物形成的ｐＨ值为５．６±０．４０。ＢＡＰ、２,４－Ｄ、ＮＡＡ或ＩＢＡ对细胞生长无显著的促进作用,且都会抑制紫草宁衍生物的形成。在生长培养基中添加１．０ｍｇ／ｌ　ＩＡＡ和０．５ｍｇ／ｌＫＴ可促进细胞生长,而在生产培养基中附加０．１ｍｇ／ｌＫＴ和０．７５─１．０ｍｇ／ｌＩＡＡ则有利于紫草宁衍生物含量及产量的提高。     

Fed-batch hairy root cultures within situ separation

Fed-batch cultures ofL. erythrorhizon hairy root were carried out by controlling sucrose concentration and media conductivity in a shake flask and a modified stirred tank reactor. For the efficient product recovery from the culture,in situ adsorption by XAD-2 was also conducted. When sucrose was used as a carbon source, the highest shikonin production and hairy root growth were obtained. When glucose or fructose was used instead, the growth was severely inhibited. In addition, it was found that alternating feeding of sucrose could be used as an effective strategy for enhancing the productivity of shikonin derivatives., As the XAD-2 amount was increased up to 1.5 g/L, shikonin production was enhanced by removing shikonin produced and other products which might be inhibitory to cell growth. Most amount of shikonin produced was successfully recovered in XAD-2 (Over 99%). Using hairy root culture in a modified stirred tank reactor, the shikonin productivity and hairy root growth rate on the average were 9.34 mg/L day and 0.49 g DCW/L · day, respectively.     

Enzyme activity and shikonin production in Lithospermum erythrorhizon cell cultures

The activities of the biosynthetic enzmes phenylalanine ammonia lyase (PAL) and 3-hydroxy-3-methylglutaryl-CoA-reductase (HMGR) were measured in cells transferred from growth to production medium in a two-stage batch culture. It was found that both these enzymes showed transient increases, PAL (three- to fourfold) and HMGR (two- to four-fold), at or near the point of exhaustion of nitrogen source (NO(3)). Production of shikonin derivatives also started at this time. The addition of excess nitrate to the medium shortly before nitrate exhaustion (days 6-8) markedly reduced the final product yield (by 70-80%) while addition of excess nitrate in the later stationary growth phase (days 14-16) had no significant effect. When the production rate of shikonin derivatives was correlated with PAL activity, it was observed that production rate is very low (less than 1 mg/L . day) at low levels of PAL activity (below 0.1 unit/mg protein). Once a threshold level of PAL activity (about 0.15 unit/mg protein) is reached, the biosynthetic rate of shikonin derivatives increases. Such a relationship could not be deduced for HMGR activity. It was concluded that the production of shikonin derivatives may be limited at the phenylalanine deaminating step at low levels of PAL activity.     

The Effective Production of Shikonin by Cultures with an Increased Cell Population

We have studied the efficient production of shikonin derivatives by suspension cultures of Lithospermum erythrorhizon with an increased cell population. The yield of shikonin derivatives was highest (800 mg/liter) when 2.8 g dry wt/liter of the cells was inoculated into the M-2 medium which we had developed for the production, but the excess inoculum lowered the yield.

We investigated suitable conditions for production with the increased cell population. The optimum amount of inoculum rose to 4.9 g dry wt/liter when the concentrations of all the components contained in the M-8 medium, which we developed for increasing the productivity by modification of the M-2 medium, were increased in proportion to the amount of inoculum, and consequently we could increase the yield of the shikonin derivatives from 1400 mg/liter to 1900 mg/liter. Moreover, the increased rate of oxygen supply in addition to the enrichment of the medium made it possible to produce 2300 mg/liter of the shikonin derivatives from a culture for which 5.6 g dry wt/liter of the cells was inoculated.     

杜仲细胞悬浮培养产黄酮及其动力学研究

本文应用正交设计对杜仲细胞悬浮培养的基本培养基和植物生长物质浓度进行了筛选,并对影响杜仲细胞悬浮培养和总黄酮含量的不同因素进行了考察。结果表明,B5培养基+0.5mg/L NAA+0.6mg/L 6-BA、蔗糖30g/L、初始pH 5.0-5.5、接种量20g(FW)/L以及摇床转速110r/min为杜仲细胞悬浮培养的适宜条件。通过对杜仲悬浮细胞生长和代谢动力学的分析表明：杜仲细胞悬浮培养生长符合Logistic生长模型,最大比生长速率( m)为0.417d-1;细胞基于蔗糖的真正比生长得率(YG)与维持系数(m)分别为0.619g/g和0.0206g/(g·d-1);黄酮合成属部分生长耦联型,可用Luedeking-Piret模型进行描述。研究结果为杜仲细胞大规模悬浮培养生产天然活性成分奠定了基础。     

建立金线莲原球茎悬浮体系生产次生代谢产物

研究植物激素浓度和培养周期对金线莲原球茎悬浮培养生长及其代谢产物积累的影响,以增加金线莲悬浮培养的生长量,提高次生代谢产物的生产。结果表明,MS培养基添加S-3307 1.0mg/L,6-BA0.5mg/L和3%的蔗糖适合总生物量的生长(214.45g/L,FW和18.23g/L DW)。而MS培养基添加S-3307 1.0mg/L,6-BA 3.0mg/L和5%的蔗糖,总黄酮,总酚和多糖的干重(5.43mg/g,2.87mg/g和243.23mg/g)达到最大化。研究原球茎悬浮培养过程,发现经过7个星期培养就能获得最大的生物质总量(225.98 g/L的FW和18.53 g/L的DW)、总黄酮干重(5.09mg/g)和总酚干重(2.04mg/g),而多糖生产达到其峰值(229.36mg/g干重)是在培养后5个星期。     

Effect of growth hormone modifications on shikonin production fromLithospermum erythrorhizon cell cultures within situ extraction

Summary The effect of growth hormone modifications on shikonin production was studied with the cell cultures ofLithospermum erythrorhizon. The cells grown in SH–H or SHA medium were effective for shikonin production in M–9 medium and maximum shikonin concentrations reached 43 and 63 mg/L, respectively, within situ extraction. In the case of the cells grown in SHA medium, induction time required for shikonin production was very short and the maximum shikonin concentration was obtained within 6 days.